US20020039962A1 - Bridged zirconocene compounds, process for their preparation and their use as catalyst components in the polymerization of olefins - Google Patents
Bridged zirconocene compounds, process for their preparation and their use as catalyst components in the polymerization of olefins Download PDFInfo
- Publication number
- US20020039962A1 US20020039962A1 US09/972,336 US97233601A US2002039962A1 US 20020039962 A1 US20020039962 A1 US 20020039962A1 US 97233601 A US97233601 A US 97233601A US 2002039962 A1 US2002039962 A1 US 2002039962A1
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- United States
- Prior art keywords
- formula
- compound
- indenyl
- bis
- group
- Prior art date
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- 238000006116 polymerization reaction Methods 0.000 title claims abstract description 43
- 239000003054 catalyst Substances 0.000 title claims abstract description 31
- 150000001336 alkenes Chemical class 0.000 title claims abstract description 14
- ZMMRKRFMSDTOLV-UHFFFAOYSA-N cyclopenta-1,3-diene zirconium Chemical class [Zr].C1C=CC=C1.C1C=CC=C1 ZMMRKRFMSDTOLV-UHFFFAOYSA-N 0.000 title claims abstract 3
- 238000000034 method Methods 0.000 title claims description 39
- 238000002360 preparation method Methods 0.000 title claims description 29
- 239000003446 ligand Substances 0.000 claims abstract description 45
- 239000001257 hydrogen Substances 0.000 claims abstract description 29
- 229910052739 hydrogen Inorganic materials 0.000 claims abstract description 29
- 125000003454 indenyl group Chemical group C1(C=CC2=CC=CC=C12)* 0.000 claims abstract description 18
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims abstract description 14
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 claims description 108
- -1 zirconocene compound Chemical class 0.000 claims description 61
- 150000001875 compounds Chemical class 0.000 claims description 52
- 239000000203 mixture Substances 0.000 claims description 52
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 claims description 45
- VPGLGRNSAYHXPY-UHFFFAOYSA-L zirconium(2+);dichloride Chemical compound Cl[Zr]Cl VPGLGRNSAYHXPY-UHFFFAOYSA-L 0.000 claims description 36
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 34
- 238000006243 chemical reaction Methods 0.000 claims description 33
- 150000002009 diols Chemical class 0.000 claims description 32
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 claims description 26
- 239000005977 Ethylene Substances 0.000 claims description 26
- WYURNTSHIVDZCO-UHFFFAOYSA-N tetrahydrofuran Substances C1CCOC1 WYURNTSHIVDZCO-UHFFFAOYSA-N 0.000 claims description 26
- 229910001868 water Inorganic materials 0.000 claims description 25
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 claims description 23
- 229920006395 saturated elastomer Polymers 0.000 claims description 21
- 239000002904 solvent Substances 0.000 claims description 19
- AQZWEFBJYQSQEH-UHFFFAOYSA-N 2-methyloxaluminane Chemical compound C[Al]1CCCCO1 AQZWEFBJYQSQEH-UHFFFAOYSA-N 0.000 claims description 18
- LIKMAJRDDDTEIG-UHFFFAOYSA-N 1-hexene Chemical compound CCCCC=C LIKMAJRDDDTEIG-UHFFFAOYSA-N 0.000 claims description 17
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 claims description 17
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 claims description 17
- 125000001424 substituent group Chemical group 0.000 claims description 17
- 239000003960 organic solvent Substances 0.000 claims description 16
- FYSNRJHAOHDILO-UHFFFAOYSA-N thionyl chloride Chemical compound ClS(Cl)=O FYSNRJHAOHDILO-UHFFFAOYSA-N 0.000 claims description 16
- 125000006736 (C6-C20) aryl group Chemical group 0.000 claims description 15
- 239000002585 base Substances 0.000 claims description 15
- 150000002431 hydrogen Chemical class 0.000 claims description 15
- 125000003837 (C1-C20) alkyl group Chemical group 0.000 claims description 14
- 125000000118 dimethyl group Chemical group [H]C([H])([H])* 0.000 claims description 14
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 12
- 230000003213 activating effect Effects 0.000 claims description 11
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 claims description 10
- 230000003197 catalytic effect Effects 0.000 claims description 10
- 229910052784 alkaline earth metal Inorganic materials 0.000 claims description 9
- 150000001342 alkaline earth metals Chemical class 0.000 claims description 9
- VSCWAEJMTAWNJL-UHFFFAOYSA-K aluminium trichloride Chemical compound Cl[Al](Cl)Cl VSCWAEJMTAWNJL-UHFFFAOYSA-K 0.000 claims description 9
- 125000004429 atom Chemical group 0.000 claims description 9
- 229910006124 SOCl2 Inorganic materials 0.000 claims description 8
- 125000001797 benzyl group Chemical group [H]C1=C([H])C([H])=C(C([H])=C1[H])C([H])([H])* 0.000 claims description 8
- 125000004432 carbon atom Chemical group C* 0.000 claims description 8
- 238000007334 copolymerization reaction Methods 0.000 claims description 8
- 229910052736 halogen Inorganic materials 0.000 claims description 8
- 150000002367 halogens Chemical class 0.000 claims description 8
- QDRKDTQENPPHOJ-UHFFFAOYSA-N sodium ethoxide Chemical compound [Na+].CC[O-] QDRKDTQENPPHOJ-UHFFFAOYSA-N 0.000 claims description 8
- 125000003178 carboxy group Chemical group [H]OC(*)=O 0.000 claims description 7
- VXNZUUAINFGPBY-UHFFFAOYSA-N 1-Butene Chemical compound CCC=C VXNZUUAINFGPBY-UHFFFAOYSA-N 0.000 claims description 6
- 229910052783 alkali metal Inorganic materials 0.000 claims description 6
- 150000001340 alkali metals Chemical class 0.000 claims description 6
- 229910052782 aluminium Inorganic materials 0.000 claims description 6
- 125000001495 ethyl group Chemical group [H]C([H])([H])C([H])([H])* 0.000 claims description 6
- 125000003392 indanyl group Chemical group C1(CCC2=CC=CC=C12)* 0.000 claims description 6
- 239000002168 alkylating agent Substances 0.000 claims description 5
- 229940100198 alkylating agent Drugs 0.000 claims description 5
- 125000000058 cyclopentadienyl group Chemical group C1(=CC=CC1)* 0.000 claims description 5
- 239000000178 monomer Substances 0.000 claims description 5
- 125000001997 phenyl group Chemical group [H]C1=C([H])C([H])=C(*)C([H])=C1[H] 0.000 claims description 5
- JOXIMZWYDAKGHI-UHFFFAOYSA-N toluene-4-sulfonic acid Chemical compound CC1=CC=C(S(O)(=O)=O)C=C1 JOXIMZWYDAKGHI-UHFFFAOYSA-N 0.000 claims description 5
- KWKAKUADMBZCLK-UHFFFAOYSA-N 1-octene Chemical compound CCCCCCC=C KWKAKUADMBZCLK-UHFFFAOYSA-N 0.000 claims description 4
- WSSSPWUEQFSQQG-UHFFFAOYSA-N 4-methyl-1-pentene Chemical compound CC(C)CC=C WSSSPWUEQFSQQG-UHFFFAOYSA-N 0.000 claims description 4
- 229910010084 LiAlH4 Inorganic materials 0.000 claims description 4
- 229910007161 Si(CH3)3 Inorganic materials 0.000 claims description 4
- 150000001450 anions Chemical class 0.000 claims description 4
- 230000001351 cycling effect Effects 0.000 claims description 4
- 150000002148 esters Chemical class 0.000 claims description 4
- 239000012280 lithium aluminium hydride Substances 0.000 claims description 4
- 125000001436 propyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])[H] 0.000 claims description 4
- 239000012279 sodium borohydride Substances 0.000 claims description 4
- 229910000033 sodium borohydride Inorganic materials 0.000 claims description 4
- 238000001149 thermolysis Methods 0.000 claims description 4
- WBZVXZGPXBXMSC-UHFFFAOYSA-N 2,5,6,6-tetrakis(2-methylpropyl)oxaluminane Chemical compound CC(C)CC1CC[Al](CC(C)C)OC1(CC(C)C)CC(C)C WBZVXZGPXBXMSC-UHFFFAOYSA-N 0.000 claims description 3
- 239000003638 chemical reducing agent Substances 0.000 claims description 3
- 125000002887 hydroxy group Chemical group [H]O* 0.000 claims description 3
- 239000007848 Bronsted acid Substances 0.000 claims description 2
- XTHFKEDIFFGKHM-UHFFFAOYSA-N Dimethoxyethane Chemical compound COCCOC XTHFKEDIFFGKHM-UHFFFAOYSA-N 0.000 claims description 2
- 239000003125 aqueous solvent Substances 0.000 claims description 2
- 125000004122 cyclic group Chemical group 0.000 claims description 2
- TVMXDCGIABBOFY-UHFFFAOYSA-N n-Octanol Natural products CCCCCCCC TVMXDCGIABBOFY-UHFFFAOYSA-N 0.000 claims description 2
- RPDAUEIUDPHABB-UHFFFAOYSA-N potassium ethoxide Chemical compound [K+].CC[O-] RPDAUEIUDPHABB-UHFFFAOYSA-N 0.000 claims description 2
- 229910000104 sodium hydride Inorganic materials 0.000 claims description 2
- 238000011282 treatment Methods 0.000 claims description 2
- 238000007257 deesterification reaction Methods 0.000 claims 1
- 238000009826 distribution Methods 0.000 abstract description 8
- YBYIRNPNPLQARY-UHFFFAOYSA-N 1H-indene Natural products C1=CC=C2CC=CC2=C1 YBYIRNPNPLQARY-UHFFFAOYSA-N 0.000 abstract description 6
- 229920001038 ethylene copolymer Polymers 0.000 abstract 1
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 83
- YMWUJEATGCHHMB-UHFFFAOYSA-N Dichloromethane Chemical compound ClCCl YMWUJEATGCHHMB-UHFFFAOYSA-N 0.000 description 61
- HEDRZPFGACZZDS-MICDWDOJSA-N Trichloro(2H)methane Chemical compound [2H]C(Cl)(Cl)Cl HEDRZPFGACZZDS-MICDWDOJSA-N 0.000 description 60
- 239000000243 solution Substances 0.000 description 59
- 238000005160 1H NMR spectroscopy Methods 0.000 description 50
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 46
- UHOVQNZJYSORNB-MZWXYZOWSA-N benzene-d6 Chemical compound [2H]C1=C([2H])C([2H])=C([2H])C([2H])=C1[2H] UHOVQNZJYSORNB-MZWXYZOWSA-N 0.000 description 36
- 239000011541 reaction mixture Substances 0.000 description 36
- YMWUJEATGCHHMB-DICFDUPASA-N dichloromethane-d2 Chemical compound [2H]C([2H])(Cl)Cl YMWUJEATGCHHMB-DICFDUPASA-N 0.000 description 32
- 238000001644 13C nuclear magnetic resonance spectroscopy Methods 0.000 description 31
- 125000003118 aryl group Chemical group 0.000 description 29
- 239000000843 powder Substances 0.000 description 29
- 230000015572 biosynthetic process Effects 0.000 description 28
- IDASTKMEQGPVRR-UHFFFAOYSA-N cyclopenta-1,3-diene;zirconium(2+) Chemical class [Zr+2].C=1C=C[CH-]C=1.C=1C=C[CH-]C=1 IDASTKMEQGPVRR-UHFFFAOYSA-N 0.000 description 27
- 238000003786 synthesis reaction Methods 0.000 description 26
- 238000003756 stirring Methods 0.000 description 23
- 229910007928 ZrCl2 Inorganic materials 0.000 description 22
- CSNNHWWHGAXBCP-UHFFFAOYSA-L Magnesium sulfate Chemical compound [Mg+2].[O-][S+2]([O-])([O-])[O-] CSNNHWWHGAXBCP-UHFFFAOYSA-L 0.000 description 16
- QNXSIUBBGPHDDE-UHFFFAOYSA-N indan-1-one Chemical compound C1=CC=C2C(=O)CCC2=C1 QNXSIUBBGPHDDE-UHFFFAOYSA-N 0.000 description 16
- 229920000642 polymer Polymers 0.000 description 16
- 239000000047 product Substances 0.000 description 16
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 14
- OFBQJSOFQDEBGM-UHFFFAOYSA-N Pentane Chemical compound CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 description 14
- UIIMBOGNXHQVGW-UHFFFAOYSA-M Sodium bicarbonate Chemical compound [Na+].OC([O-])=O UIIMBOGNXHQVGW-UHFFFAOYSA-M 0.000 description 14
- 239000000725 suspension Substances 0.000 description 14
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 12
- 239000010410 layer Substances 0.000 description 12
- MZRVEZGGRBJDDB-UHFFFAOYSA-N n-Butyllithium Substances [Li]CCCC MZRVEZGGRBJDDB-UHFFFAOYSA-N 0.000 description 12
- DLEDOFVPSDKWEF-UHFFFAOYSA-N lithium butane Chemical compound [Li+].CCC[CH2-] DLEDOFVPSDKWEF-UHFFFAOYSA-N 0.000 description 11
- 239000007787 solid Substances 0.000 description 11
- KXHNSSHBYAVFMS-UHFFFAOYSA-N 2-[2-(1h-inden-2-yl)ethyl]-1h-indene Chemical compound C1=CC=C2CC(CCC=3CC4=CC=CC=C4C=3)=CC2=C1 KXHNSSHBYAVFMS-UHFFFAOYSA-N 0.000 description 10
- 238000005481 NMR spectroscopy Methods 0.000 description 10
- 229910007932 ZrCl4 Inorganic materials 0.000 description 10
- WYURNTSHIVDZCO-SVYQBANQSA-N deuterated tetrahydrofuran Substances [2H]C1([2H])OC([2H])([2H])C([2H])([2H])C1([2H])[2H] WYURNTSHIVDZCO-SVYQBANQSA-N 0.000 description 10
- DUNKXUFBGCUVQW-UHFFFAOYSA-J zirconium tetrachloride Chemical compound Cl[Zr](Cl)(Cl)Cl DUNKXUFBGCUVQW-UHFFFAOYSA-J 0.000 description 10
- OTMSDBZUPAUEDD-UHFFFAOYSA-N Ethane Chemical compound CC OTMSDBZUPAUEDD-UHFFFAOYSA-N 0.000 description 9
- 0 CC.CC.CC.CC.CC(C)(c1cc2ccccc2c1)C(C)(C)c1cc2ccccc2c1.C[Zr](C)C Chemical compound CC.CC.CC.CC.CC(C)(c1cc2ccccc2c1)C(C)(C)c1cc2ccccc2c1.C[Zr](C)C 0.000 description 8
- IMNFDUFMRHMDMM-UHFFFAOYSA-N N-Heptane Chemical compound CCCCCCC IMNFDUFMRHMDMM-UHFFFAOYSA-N 0.000 description 8
- 230000000694 effects Effects 0.000 description 8
- 239000000543 intermediate Substances 0.000 description 8
- 229910052943 magnesium sulfate Inorganic materials 0.000 description 8
- 239000002244 precipitate Substances 0.000 description 8
- MCULRUJILOGHCJ-UHFFFAOYSA-N triisobutylaluminium Chemical compound CC(C)C[Al](CC(C)C)CC(C)C MCULRUJILOGHCJ-UHFFFAOYSA-N 0.000 description 8
- 229910052726 zirconium Inorganic materials 0.000 description 8
- UMGHCEPAQJUHNV-UHFFFAOYSA-N 2,5-dibenzylhexanedioic acid Chemical compound C=1C=CC=CC=1CC(C(=O)O)CCC(C(O)=O)CC1=CC=CC=C1 UMGHCEPAQJUHNV-UHFFFAOYSA-N 0.000 description 7
- QSZIHBKUAAAXMD-UHFFFAOYSA-N 2-[2-(1,3-dimethyl-1h-inden-2-yl)ethyl]-1,3-dimethyl-1h-indene Chemical compound C1=CC=C2C(C)C(CCC=3C(C4=CC=CC=C4C=3C)C)=C(C)C2=C1 QSZIHBKUAAAXMD-UHFFFAOYSA-N 0.000 description 7
- 238000012512 characterization method Methods 0.000 description 7
- 238000001816 cooling Methods 0.000 description 7
- 229920001577 copolymer Polymers 0.000 description 7
- 229910052757 nitrogen Inorganic materials 0.000 description 7
- 238000010992 reflux Methods 0.000 description 7
- 229910000030 sodium bicarbonate Inorganic materials 0.000 description 7
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 6
- 239000012047 saturated solution Substances 0.000 description 6
- 239000011780 sodium chloride Substances 0.000 description 6
- MWZYHHNUNXLIIG-UHFFFAOYSA-N 2-[2-(3-oxo-7-phenyl-1,2-dihydroinden-2-yl)ethyl]-4-phenyl-2,3-dihydroinden-1-one Chemical compound C1C(C(=CC=C2)C=3C=CC=CC=3)=C2C(=O)C1CCC(C1=O)CC2=C1C=CC=C2C1=CC=CC=C1 MWZYHHNUNXLIIG-UHFFFAOYSA-N 0.000 description 5
- 238000004458 analytical method Methods 0.000 description 5
- 239000007864 aqueous solution Substances 0.000 description 5
- 238000002425 crystallisation Methods 0.000 description 5
- 230000008025 crystallization Effects 0.000 description 5
- 239000011521 glass Substances 0.000 description 5
- 239000012044 organic layer Substances 0.000 description 5
- 239000002002 slurry Substances 0.000 description 5
- 238000010561 standard procedure Methods 0.000 description 5
- 238000005406 washing Methods 0.000 description 5
- IBKNFVLKFMWWCR-UHFFFAOYSA-N 1-methyl-2-[2-(1-methyl-1h-inden-2-yl)ethyl]-1h-indene Chemical compound C1=CC=C2C(C)C(CCC=3C(C4=CC=CC=C4C=3)C)=CC2=C1 IBKNFVLKFMWWCR-UHFFFAOYSA-N 0.000 description 4
- DDHOUKOWIVVYPE-UHFFFAOYSA-N 2,5-dibenzylhexanedioyl dichloride Chemical compound C=1C=CC=CC=1CC(C(=O)Cl)CCC(C(Cl)=O)CC1=CC=CC=C1 DDHOUKOWIVVYPE-UHFFFAOYSA-N 0.000 description 4
- 241000349731 Afzelia bipindensis Species 0.000 description 4
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 4
- QCWXUUIWCKQGHC-UHFFFAOYSA-N Zirconium Chemical compound [Zr] QCWXUUIWCKQGHC-UHFFFAOYSA-N 0.000 description 4
- KCXMKQUNVWSEMD-UHFFFAOYSA-N benzyl chloride Chemical compound ClCC1=CC=CC=C1 KCXMKQUNVWSEMD-UHFFFAOYSA-N 0.000 description 4
- 229940073608 benzyl chloride Drugs 0.000 description 4
- 230000000052 comparative effect Effects 0.000 description 4
- HWWXKBXLPYSRNO-UHFFFAOYSA-N diethyl 2,5-bis[(2-phenylphenyl)methyl]hexanedioate Chemical compound C=1C=CC=C(C=2C=CC=CC=2)C=1CC(C(=O)OCC)CCC(C(=O)OCC)CC1=CC=CC=C1C1=CC=CC=C1 HWWXKBXLPYSRNO-UHFFFAOYSA-N 0.000 description 4
- 238000001035 drying Methods 0.000 description 4
- 239000007789 gas Substances 0.000 description 4
- KWGKDLIKAYFUFQ-UHFFFAOYSA-M lithium chloride Chemical compound [Li+].[Cl-] KWGKDLIKAYFUFQ-UHFFFAOYSA-M 0.000 description 4
- IHLVCKWPAMTVTG-UHFFFAOYSA-N lithium;carbanide Chemical compound [Li+].[CH3-] IHLVCKWPAMTVTG-UHFFFAOYSA-N 0.000 description 4
- 238000000746 purification Methods 0.000 description 4
- PBKONEOXTCPAFI-UHFFFAOYSA-N 1,2,4-trichlorobenzene Chemical compound ClC1=CC=C(Cl)C(Cl)=C1 PBKONEOXTCPAFI-UHFFFAOYSA-N 0.000 description 3
- RFFLAFLAYFXFSW-UHFFFAOYSA-N 1,2-dichlorobenzene Chemical compound ClC1=CC=CC=C1Cl RFFLAFLAYFXFSW-UHFFFAOYSA-N 0.000 description 3
- IDQFTFSTYVWBIZ-UHFFFAOYSA-N 1-ethyl-2-[2-(1-ethyl-1h-inden-2-yl)ethyl]-1h-indene Chemical compound C1=CC=C2C(CC)C(CCC=3C(C4=CC=CC=C4C=3)CC)=CC2=C1 IDQFTFSTYVWBIZ-UHFFFAOYSA-N 0.000 description 3
- GNXQGFGJDYUKFU-UHFFFAOYSA-N 1-methyl-2-[2-(1-methyl-4-phenyl-1h-inden-2-yl)ethyl]-4-phenyl-1h-indene Chemical compound C=1C(C(=CC=C2)C=3C=CC=CC=3)=C2C(C)C=1CCC(C1C)=CC2=C1C=CC=C2C1=CC=CC=C1 GNXQGFGJDYUKFU-UHFFFAOYSA-N 0.000 description 3
- VBDPXNNRCIXHFT-UHFFFAOYSA-N 2-(1h-inden-2-ylmethyl)-1h-indene Chemical compound C1=CC=C2CC(CC=3CC4=CC=CC=C4C=3)=CC2=C1 VBDPXNNRCIXHFT-UHFFFAOYSA-N 0.000 description 3
- UBKJRUPGXCPDBI-UHFFFAOYSA-N 4-phenyl-2-[2-(4-phenyl-1-propan-2-yl-1h-inden-2-yl)ethyl]-1-propan-2-yl-1h-indene Chemical compound C=1C(C(=CC=C2)C=3C=CC=CC=3)=C2C(C(C)C)C=1CCC(C1C(C)C)=CC2=C1C=CC=C2C1=CC=CC=C1 UBKJRUPGXCPDBI-UHFFFAOYSA-N 0.000 description 3
- CWUFYNOKNSOWEV-UHFFFAOYSA-N 4-phenyl-2-[2-(4-phenyl-1h-inden-2-yl)ethyl]-1h-indene Chemical compound C=1C(C(=CC=C2)C=3C=CC=CC=3)=C2CC=1CCC(C1)=CC2=C1C=CC=C2C1=CC=CC=C1 CWUFYNOKNSOWEV-UHFFFAOYSA-N 0.000 description 3
- FXLAIQOPPNYFAH-UHFFFAOYSA-N C#COOC(Cc1ccccc1)C(C)(C)C(C)(C)C(Cc1ccccc1)C(=O)OC.CC.CC.[V] Chemical compound C#COOC(Cc1ccccc1)C(C)(C)C(C)(C)C(Cc1ccccc1)C(=O)OC.CC.CC.[V] FXLAIQOPPNYFAH-UHFFFAOYSA-N 0.000 description 3
- 239000004215 Carbon black (E152) Substances 0.000 description 3
- VIZORQUEIQEFRT-UHFFFAOYSA-N Diethyl adipate Chemical compound CCOC(=O)CCCCC(=O)OCC VIZORQUEIQEFRT-UHFFFAOYSA-N 0.000 description 3
- KWYHDKDOAIKMQN-UHFFFAOYSA-N N,N,N',N'-tetramethylethylenediamine Chemical compound CN(C)CCN(C)C KWYHDKDOAIKMQN-UHFFFAOYSA-N 0.000 description 3
- 230000002378 acidificating effect Effects 0.000 description 3
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 3
- 238000005119 centrifugation Methods 0.000 description 3
- HQQADJVZYDDRJT-UHFFFAOYSA-N ethene;prop-1-ene Chemical group C=C.CC=C HQQADJVZYDDRJT-UHFFFAOYSA-N 0.000 description 3
- 239000000284 extract Substances 0.000 description 3
- 229920001519 homopolymer Polymers 0.000 description 3
- 229930195733 hydrocarbon Natural products 0.000 description 3
- 150000002430 hydrocarbons Chemical class 0.000 description 3
- 238000005259 measurement Methods 0.000 description 3
- 238000002844 melting Methods 0.000 description 3
- 230000008018 melting Effects 0.000 description 3
- 229910052751 metal Inorganic materials 0.000 description 3
- 239000002184 metal Substances 0.000 description 3
- 239000002808 molecular sieve Substances 0.000 description 3
- 238000001542 size-exclusion chromatography Methods 0.000 description 3
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 description 3
- XZIKSWMNFLIAQP-UHFFFAOYSA-N tris(2,4,4-trimethylpentyl)alumane Chemical compound CC(C)(C)CC(C)C[Al](CC(C)CC(C)(C)C)CC(C)CC(C)(C)C XZIKSWMNFLIAQP-UHFFFAOYSA-N 0.000 description 3
- SEXZHJJUKFXNDY-UHFFFAOYSA-N 1-(bromomethyl)-2-phenylbenzene Chemical compound BrCC1=CC=CC=C1C1=CC=CC=C1 SEXZHJJUKFXNDY-UHFFFAOYSA-N 0.000 description 2
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- 150000003839 salts Chemical class 0.000 description 1
- 238000006748 scratching Methods 0.000 description 1
- 230000002393 scratching effect Effects 0.000 description 1
- 238000010583 slow cooling Methods 0.000 description 1
- 241000894007 species Species 0.000 description 1
- 230000000087 stabilizing effect Effects 0.000 description 1
- 239000007858 starting material Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 239000000758 substrate Substances 0.000 description 1
- 238000002076 thermal analysis method Methods 0.000 description 1
- 229910052723 transition metal Inorganic materials 0.000 description 1
- 150000003624 transition metals Chemical class 0.000 description 1
- MCWWHQMTJNSXPX-UHFFFAOYSA-N tribenzylalumane Chemical compound C=1C=CC=CC=1C[Al](CC=1C=CC=CC=1)CC1=CC=CC=C1 MCWWHQMTJNSXPX-UHFFFAOYSA-N 0.000 description 1
- JLTRXTDYQLMHGR-UHFFFAOYSA-N trimethylaluminium Chemical compound C[Al](C)C JLTRXTDYQLMHGR-UHFFFAOYSA-N 0.000 description 1
- CFCIWEFTNUMUJY-UHFFFAOYSA-N tris(2-methylphenyl)alumane Chemical compound CC1=CC=CC=C1[Al](C=1C(=CC=CC=1)C)C1=CC=CC=C1C CFCIWEFTNUMUJY-UHFFFAOYSA-N 0.000 description 1
- MLDSMTVYPPIXMZ-UHFFFAOYSA-N tris(4-methylpentyl)alumane Chemical compound CC(C)CCC[Al](CCCC(C)C)CCCC(C)C MLDSMTVYPPIXMZ-UHFFFAOYSA-N 0.000 description 1
- PXXNTAGJWPJAGM-UHFFFAOYSA-N vertaline Natural products C1C2C=3C=C(OC)C(OC)=CC=3OC(C=C3)=CC=C3CCC(=O)OC1CC1N2CCCC1 PXXNTAGJWPJAGM-UHFFFAOYSA-N 0.000 description 1
- 239000003643 water by type Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C67/00—Preparation of carboxylic acid esters
- C07C67/30—Preparation of carboxylic acid esters by modifying the acid moiety of the ester, such modification not being an introduction of an ester group
- C07C67/333—Preparation of carboxylic acid esters by modifying the acid moiety of the ester, such modification not being an introduction of an ester group by isomerisation; by change of size of the carbon skeleton
- C07C67/343—Preparation of carboxylic acid esters by modifying the acid moiety of the ester, such modification not being an introduction of an ester group by isomerisation; by change of size of the carbon skeleton by increase in the number of carbon atoms
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C13/00—Cyclic hydrocarbons containing rings other than, or in addition to, six-membered aromatic rings
- C07C13/28—Polycyclic hydrocarbons or acyclic hydrocarbon derivatives thereof
- C07C13/32—Polycyclic hydrocarbons or acyclic hydrocarbon derivatives thereof with condensed rings
- C07C13/45—Polycyclic hydrocarbons or acyclic hydrocarbon derivatives thereof with condensed rings with a bicyclo ring system containing nine carbon atoms
- C07C13/465—Indenes; Completely or partially hydrogenated indenes
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C69/00—Esters of carboxylic acids; Esters of carbonic or haloformic acids
- C07C69/612—Esters of carboxylic acids having a carboxyl group bound to an acyclic carbon atom and having a six-membered aromatic ring in the acid moiety
- C07C69/616—Esters of carboxylic acids having a carboxyl group bound to an acyclic carbon atom and having a six-membered aromatic ring in the acid moiety polycyclic
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07F—ACYCLIC, CARBOCYCLIC OR HETEROCYCLIC COMPOUNDS CONTAINING ELEMENTS OTHER THAN CARBON, HYDROGEN, HALOGEN, OXYGEN, NITROGEN, SULFUR, SELENIUM OR TELLURIUM
- C07F17/00—Metallocenes
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F10/00—Homopolymers and copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2602/00—Systems containing two condensed rings
- C07C2602/02—Systems containing two condensed rings the rings having only two atoms in common
- C07C2602/04—One of the condensed rings being a six-membered aromatic ring
- C07C2602/08—One of the condensed rings being a six-membered aromatic ring the other ring being five-membered, e.g. indane
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F110/00—Homopolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
- C08F110/02—Ethene
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F110/00—Homopolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
- C08F110/04—Monomers containing three or four carbon atoms
- C08F110/06—Propene
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F210/00—Copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
- C08F210/16—Copolymers of ethene with alpha-alkenes, e.g. EP rubbers
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F4/00—Polymerisation catalysts
- C08F4/42—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors
- C08F4/44—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides
- C08F4/60—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides together with refractory metals, iron group metals, platinum group metals, manganese, rhenium technetium or compounds thereof
- C08F4/62—Refractory metals or compounds thereof
- C08F4/64—Titanium, zirconium, hafnium or compounds thereof
- C08F4/659—Component covered by group C08F4/64 containing a transition metal-carbon bond
- C08F4/65912—Component covered by group C08F4/64 containing a transition metal-carbon bond in combination with an organoaluminium compound
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S526/00—Synthetic resins or natural rubbers -- part of the class 520 series
- Y10S526/943—Polymerization with metallocene catalysts
Definitions
- the present invention relates to bridged zirconocene compounds, to the corresponding ligands, to a new process for their preparation and to the use of said zirconocenes as catalytic components in the polymerization of olefins.
- the indenyl groups are linked together by divalent radicals containing one or more carbon atoms and/or heteroatoms; the divalent bridging groups are generally linked to the 1 position of said indenyl groups, and therefore, the common indenyl metallocenes are 1-indenyl compounds.
- the European patent application EP 0 485 823 describes a class of bridged bis(1-indenyl) metallocenes, wherein the indenyl groups have a substituent other than hydrogen in the 2 position and are bridged in the 1 position by means of a bridge containing 1 or more carbon atoms (e.g. an ethylene or isopropylidene group) or containing heteroatoms (e.g. a dimethyl-silyl or a diphenyl-silyl group).
- a bridge containing 1 or more carbon atoms e.g. an ethylene or isopropylidene group
- heteroatoms e.g. a dimethyl-silyl or a
- the European patent application EP 0 372 414 describes a very broad class of bridged or unbridged metallocenes; among the many metallocenes exemplified, are reported two specific bis-indenyl metallocene compounds, wherein the divalent group bridging the indenyl groups is linked to the 1 position of one indenyl group and to the 2 position of the other indenyl group (formulae II-1 and II-2, on page 5 of said patent application).
- the International patent application WO 94/11406 describes a very broad class of metallocene compounds of formula R′Ind-M-(CP)Q k , wherein: Ind is an indenyl group; R′ is a substituent, other than hydrogen, linked in the 2 position of said indenyl group; Cp is a cyclopentadienyl group; M is a transition metal belonging to group 3, 4, 5 or 6 of the Periodic Table of Elements; and Q is a ⁇ -ligand of the metal M, k being an integer linked to the valence of said metal M.
- R′ can form a bridge between the 2 position of the Ind group and the Cp group of the above formula; therefore, the class of bis(2-indenyl) compounds is generically described.
- bridging group R′ is very broad too, the preferred bridges linking the two indenyl residues being —S—, (CH 3 ) 2 Si ⁇ and —CH 2 — groups; in fact, in the working examples only bis-indenyl zirconocenes with a one-atom-bridge have actually been synthesized and tested in ethylene (co)polymerization, giving ethylene homopolymers in very low yield and ethylene/propylene copolymers having very low molecular weights and in low yields too.
- the Applicant has now unexpectedly found a new class of bridged bis(2-indenyl)zirconocenes, particularly active as catalyst components for the polymerization of olefins.
- Said zirconocene compounds are characterized by the presence of two indenyl ligands, bridged in the 2 position by means of a two-carbon-atoms divalent group.
- an object of the present invention is a bridged zirconocene compound of formula (I):
- R 1 , R 2 , R 3 and R 4 are selected from the group consisting of hydrogen, linear or branched, saturated or unsaturated, C 1 -C 20 alkyl, C 3 -C 20 cycloalkyl, C 6 -C 20 aryl, C 7 -C 20 alkylaryl and C 7 -C 20 arylalkyl radicals, optionally containing one or more Si or Ge atoms, or wherein two substituents of R 1 , R 2 , R 3 and R 4 form a ring having from 4 to 8 carbon atoms;
- R 5 and R 6 are selected from the group consisting of linear or branched, saturated or unsaturated C 1 -C 20 alkyl, C 3 -C 20 cycloalkyl, C 6 -C 20 aryl, C 7 -C 20 alkylaryl and C 7 -C 20 arylalkyl radicals, optionally containing one or more Si or Ge atoms, or two vicinal R 6 substituents on the same indenyl group form a ring having from 4 to 8 carbon atoms;
- the groups X are hydrogen, halogen, —R, —OR, —SR, —NR 2 or —PR 2 , wherein R is selected from the group consisting of linear or branched, saturated or unsaturated, C 1 -C 20 alkyl, C 3 -C 20 cycloalkyl, C 6 -C 20 aryl, C 7 -C 20 alkylaryl and C 7 -C 20 arylalkyl radicals, optionally containing one or more Si or Ge atoms.
- Another object of the present invention is a catalyst for the polymerization of olefins comprising the product obtainable by contacting:
- the present invention provides a process for the polymerization of olefins comprising the polymerization reaction of one or more olefinic monomers in the presence of a catalyst as described above.
- Another object of the present invention is a ligand of formula (II):
- R 1 , R 2 , R 3 , R 4 , R 5 and R 6 , m and n have the meaning reported above, with the proviso that:
- R 1 , R 2 , R 3 and R 4 are hydrogen, n is 0 and m is 1, then R 5 is different from —CH 3 , —CH 2 Ph and —Si(CH 3 ) 3 .
- the present invention further concerns a process for the preparation of the above ligands of formula (II), comprising the following steps:
- R 1 , R 2 , R 3 , R 4 , R 6 and n have the meaning reported above
- R 7 is selected from the group consisting of linear or branched, saturated or unsaturated C 1 -C 20 alkyl, C 3 -C 20 cycloalkyl, C 6 -C 20 aryl, C 7 -C 20 alkylaryl and C 7 -C 20 arylalkyl radicals
- Y is a suitable leaving group
- R 1 , R 2 , R 3 , R 4 , R 6 and n have the meaning reported above and Y′ is a suitable leaving group
- R 1 , R 2 , R 3 , R 4 , R 6 and n have the meaning reported above.
- the substituents R 5 can be introduced on the cyclopentadienyl ring by reacting a compound of formula (VII) or the same ligand of formula (II) with a suitable amount of an alkylating agent R 5 MgBr, R 5 MgCl or R 5 j B, wherein B is an alkaline or alkaline-earth metal, and j is 1 or 2.
- the present invention concerns intermediate compounds of formula (V), as reported above, useful in the synthesis of the ligands (II), according to the present invention.
- R 1 , R 2 , R 3 and R 4 are selected from the group consisting of hydrogen, linear or branched, saturated or unsaturated, C 1 -C 20 alkyl, C 3 -C 20 cycloalkyl, C 6 -C 20 aryl, C 7 -C 20 alkylaryl and C 7 -C 20 arylalkyl radicals, optionally containing one or more Si or Ge atoms, or wherein two substituents of R 1 , R 2 , R 3 and R 4 form a ring having from 4 to 8 carbon atoms.
- R 1 , R 2 , R 3 and R 4 are selected from the group consisting of hydrogen, methyl, ethyl, propyl, phenyl and benzyl; more preferably, R 1 , R 2 , R 3 and R 4 are hydrogen and the bridging group of the two 2-indenyl groups is ethylene.
- R 5 and R 6 are selected from the group consisting of linear or branched, saturated or unsaturated C 1 -C 20 alkyl, C 3 -C 20 cycloalkyl, C 6 -C 20 aryl, C 7 -C 20 alkylaryl and C 7 -C 20 arylalkyl radicals, optionally containing one or more Si or Ge atoms; or two vicinal R 6 substituents on the same indenyl group form a ring having from 4 to 8 carbon atoms.
- R 5 and R 6 are preferably selected from the group consisting of methyl, ethyl, propyl, phenyl and benzyl.
- the groups X are hydrogen, halogen, —R, —OR, —SR, —NR 2 or —PR 2 , wherein R is selected from the group consisting of linear or branched, saturated or unsaturated, C 1 -C 20 alkyl, C 3 -C 20 cycloalkyl, C 6 -C 20 aryl, C 7 -C 20 alkylaryl and C 7 -C 20 arylalkyl radicals, optionally containing one or more Si or Ge atoms.
- X is preferably Cl, Br or methyl.
- bridged zirconocene compounds according to the present invention are:
- Said bridged zirconocene compounds can be prepared by reaction of the corresponding ligands of formula (II) first with a compound capable of forming a delocalized anion on the cyclopentadienyl ring, and then with a compound of formula ZrZ 4 , wherein the substituents Z, the same or different from each other, are halogen (ZrCl 4 is particularly preferred), according to common procedures known in the state of the art.
- R 1 , R 2 , R 3 and R 4 are hydrogen, n is 0 and m is 1, then R 5 is different from —CH 3 , —CH 2 Ph and —Si(CH 3 ) 3 .
- ethylene-bridged bis-2-indenyl ligands unsubstituted or bearing a substituent —CH 3 , —CH 2 Ph or —Si(CH 3 ) 3 have been disclosed by Nantz M. H. et al. in Organometallics 1993, 12:5012-5015 and by Hitchcock S. R. et al. in Organometallics 1995, 14:3732-3740.
- These ligands were used to prepare the corresponding titanocene dichloride, useful in the catalytic epoxidation of unfunctionalized alkenes.
- the ligands mentioned above are expressly excluded from the ligands according to the present invention.
- the ligands of formula (II), according to the present invention are prepared by means of a very simple and efficient process, which employs cheap starting materials and comprises single reaction steps having very high yields, some of them almost quantitative. Furthermore, said process does not require laborious and time-consuming purification procedures, being particularly suitable to large scale production.
- the process step (1) comprises reacting the adipic ester of formula (III) with at least 2 equivalents, and preferably 2-4 equivalents of a benzyl compound of formula (IV) and at least 2 equivalents, and preferably 24 equivalents of an alkali metal or alkaline earth metal base, according to the reaction scheme reported in the summary of the invention, to obtain an intermediate compound of formula (V).
- Said reaction is preferably carried out one pot, by sequential addition of said base and of the benzyl compound of formula (IV), in the presence of an organic solvent, at a temperature preferably ranging from 20 to 80° C., and more preferably from 50 to 70° C.
- Said base of an alkali metal or alkaline earth metal is preferably selected from the group consisting of NaOEt, KOEt, KOH, NaOH, NaH, KH and mixtures thereof.
- Said organic solvent is preferably selected from the group consisting of THF, glyme, toluene and mixtures thereof.
- Y is preferably Cl or Br.
- Reaction step (2) comprises cycling the compound of formula (V), according to the reaction scheme reported in the summary of the invention, to obtain a compound of formula (VII).
- said step is conducted first de-esterifying the functions —COOR 7 of the compound of formula (V) to the corresponding —COOH groups, by adding at least 2 equivalents, and preferably 2-3 equivalents, of a base in a mixture of aqueous and organic solvent.
- Said base is preferably KOH and/or NaOH.
- Said mixture of solvents is preferably a mixture of MeOH and water.
- the present reaction step is preferably carried out at a temperature ranging from 20 to 150° C., and more preferably from 70 to 100° C., for a time of 1-5 hours, and more preferably for 2-3 hours.
- the obtained diacid can be isolated by acidification, according to procedures known in the state of the art, and is subsequently derivatized with a suitable leaving group Y′, to give a compound of formula (VI).
- Said group Y′ is preferably Cl or Br.
- the compound of formula (VI) can be obtained from the above mentioned diacid by reaction with SOCl 2 in excess, and preferably in amounts ranging from 6 to 10 equivalents per leaving group Y′, at a temperature preferably ranging from 20 to 80° C., and more preferably from 50 to 60° C., for a period preferably of 4-12 hours, and more preferably of 7-9 hours.
- the compound of formula (VI) is then cycled to give the final compound (VII), in the presence of at least 1 equivalent of a Lewis acid, and preferably 1.1-1.3 equivalents of AlCl 3 , at a temperature preferably ranging from 0 and 40° C., in the presence of an organic solvent.
- the compound (VII) can be finally isolated from the reaction mixture according to standard procedures.
- Reaction step (3) comprises reducing the ketonic functions on the indanyl moieties of the compound of formula (VII) to obtain the diol (VIII) and finally dehydrating the hydroxy functions on the indanyl moieties of said diol (VIII) to give the ligand (II), according to the reaction scheme reported in the summary of the invention.
- the compound (VII) can be reduced to the diol (VIII) by reaction with at least 0.5 equivalents, and preferably 1-1.2 equivalents, of a suitable reducing agent, in an organic solvent.
- Said reducing agent is preferably selected from the group consisting of NaBH 4 , LiAlH 4 , NaH and KH; said organic solvent is preferably MeOH.
- This reaction is preferably carried out at a temperature ranging from ⁇ 20° C. to 20° C., for a time of 10-18 hours.
- the diol (VIII) can be then isolated by acidification, according to procedures known in the state of the art.
- Said diol (VIII) is subsequently dehydrated to the ligand (II) by acid treatment or by thermolysis; in the former case, the diol (VIII) is preferably treated with catalytic amounts of an acid, more preferably p-toluensulfonic acid or HCl, in an organic solvent such as ether, toluene and CH 2 Cl 2 , at a temperature ranging from 20 to 100° C. In the latter case, the diol (VIII) is preferably dehydrated by thermolysis at a temperature ranging from 200 to 300° C., and more preferably from 250 to 270° C., for a period of 1-2 hours.
- an acid more preferably p-toluensulfonic acid or HCl
- organic solvent such as ether, toluene and CH 2 Cl 2
- the final ligand (II) can be then isolated according to standard procedures known in the state of the art.
- the substituents R 5 can be introduced on the cyclopentadienyl ring by reacting a compound of formula (VII) or the same ligand of formula (II) with a suitable amount of an alkylating agent R 5 MgX′ or R 5 j B, wherein, X′ is halogen, B is an alkaline or alkaline-earth metal and j is 1 or 2.
- the compound of formula (VII) or (II) is reacted with at least 2 equivalents of said alkylating agent, at a temperature ranging from ⁇ 78° C. to 20° C., for a time of 1-3 hours.
- the reaction is preferably conducted in an organic solvent selected from the group consisting of THF, Et 2 O, toluene and mixtures thereof.
- Said alkylating agent is preferably selected from the group consisting of R 5 MgBr, R 5 MgCl, R 5 Li, R 5 2 Mg and R 5 2 Zn.
- the ligands of formula (II) according to the present invention can be easily transformed into the corresponding zirconocenes by using standard procedures known in the state of the art.
- Another object of the present invention are intermediate compounds of formula (V), useful in the synthesis of the ligands of formula (II):
- R 1 , R 2 , R 3 , R 4 , R 5 , R 6 , R 7 and n have the meaning reported above.
- the bridged zirconocene compounds according to the present invention can be advantageously used as catalytic components for the polymerization of olefins. Therefore, another object of the present invention is a catalyst for the polymerization of olefins, comprising the product obtainable by contacting the following components:
- Activating cocatalysts suitable as component (B) in the catalysts of the invention are linear, branched or cyclic alumoxanes, containing at least one group of the type:
- substituents R 8 are linear or branched, saturated or unsaturated C 1 -C 20 alkyl, C 3 -C 20 cycloalkyl, C 6 -C 20 aryl, C 7 -C 20 alkylaryl, C 7 -C 20 arylalkyl radicals, or groups —O—Al(R 8 ) 2 .
- alumoxanes suitable as activating cocatalysts in the catalysts according to the present invention are methylalumoxane (MAO), tetra-isobutyl-alumoxane (TIBAO), tetra-2,4,4-trimethylpentylalumoxane (TIOAO) and tetra-2-methyl-pentylalumoxane. Mixtures of different alumoxanes can also be used.
- Activating cocatalysts suitable as component (B) in the catalysts of the invention are also the products of the reaction between water and organometallic aluminum compounds, preferably of formula AlR 8 3 or Al 2 R 8 6 , wherein R 8 has the meaning reported above.
- organometallic aluminum compounds of formula (II) described in EP-A-575,875 and those of formula (II) described in WO 96/02580 are:
- Particularly preferred aluminum compounds are tris(2,4,4-trimethylpentyl)aluminum (TIOA), and triisobutylaluminum (TIBA).
- the molar ratio between aluminum and the metal of the zirconocene is preferably comprised between about 10:1 and about 50,000:1, and preferably between about 100:1 and about 4,000:1.
- Further activating cocatalysts suitable as component (B) in the catalysts of the invention are those compounds capable of forming an alkyl zirconocene cation.
- Non-limiting examples of these compounds are those of formula Y + Z ⁇ , wherein Y + is a Bronsted acid capable of donating a proton and of reacting irreversibly with a substituent X of the compound of formula (I), and Z ⁇ is a compatible anion which does not coordinate, which is capable of stabilizing the active catalytic species originating from the reaction of the two compounds, and which is sufficiently labile to be able to be displaced from an olefinic substrate.
- the Z ⁇ anion preferably comprises one or more boron atoms.
- the Z ⁇ anion is an anion of formula BAr 4 ( ⁇ ) , wherein the Ar substituents, the same or different from each other, are aryl radicals such as phenyl, pentafluorophenyl, bis(trifluoromethyl)phenyl. Tetrakis-pentafluorophenyl-borate is particularly preferred.
- compounds of formula BAr 3 can be used conveniently.
- the catalysts of the present invention can also be used on inert supports. This is achieved by depositing the zirconocene compound (A), or the product of its reaction with the activating cocatalyst (B), or component (B) and then the zirconocene compound (A), on inert supports such as silica, alumina or olefin polymers or prepolymer such as polyethylenes, polypropylenes or styrene-divinylbenzene copolymers.
- inert supports such as silica, alumina or olefin polymers or prepolymer such as polyethylenes, polypropylenes or styrene-divinylbenzene copolymers.
- the present invention also provides a process for the polymerization of olefins comprising the reaction of polymerization of one or more olefinic monomers in the presence of a catalyst as described above.
- olefinic monomers which may be used in the polymerization process of the invention are ethylene, ⁇ -olefins such as propylene and 1-butene, cycloolefins and conjugated diolefins.
- the catalysts of the invention can be advantageously used in ethylene homopolymerization or in the copolymerization of ethylene with propylene, 1-butene, 1-hexene, 4-methyl-1-pentene or 1-octene. Said catalysts unexpectedly allow to obtain, in high yields, ethylene polymers having very low molecular weights and having narrow molecular weight distributions (MWDs), without the need of using substantial amounts of molecular weight regulators, such as hydrogen.
- MWDs molecular weight distributions
- the catalysts of the invention it is possible to obtain, with high yields and without the use of molecular weight regulators, ethylene homopolymers or ethylene/ ⁇ -olefin copolymers having intrinsic viscosities (I.V.) lower than 1.0 dl/g, preferably comprised between 0.2 and 0.8 dl/g, more preferably between 0.3 and 0.7 dl/g; furthermore, the obtained polymers have a molecular weight distribution MWD (Mw/Mn) lower than 3.
- I.V. intrinsic viscosities
- the catalysts of the invention not always show satisfactory activities in the homopolymerization of propylene to give atactic propylene oligomers. However, when the homopolymerization of propylene is performed in the presence of hydrogen, a very large increase in the activities is unexpectedly observed.
- the present invention provides a process for propylene homopolymerization, carried out in the presence of controlled amounts of hydrogen, which lead to a significant 100-500 fold increase in homopolymerization activity.
- the amount of hydrogen is preferably comprised between 1 mol % and 30 mol %, with respect to the total quantity of hydrogen and propylene, at the temperature of 50° C.; said amount of hydrogen is more preferably 2-3 mol % of a total amount of hydrogen and propylene.
- the polymerization process according to the present invention can be carried out in the liquid phase, in the presence or absence of an inert hydrocarbon solvent, or in the gas phase.
- the hydrocarbon solvent can be either aromatic, such as toluene, or aliphatic, such as propane, hexane, heptane, isobutane and cyclohexane.
- the polymerization temperature is generally comprised between ⁇ 100° C. and +250° C., and more particularly between ⁇ 50° C. and +100° C. The lower is the polymerization temperature, the higher are the molecular weights of the polymers obtained.
- the molecular weight of the polymers can be further varied by changing the type or the concentration of the catalytic components or by using molecular weight regulators, for example hydrogen. Nevertheless, we stress again that the gist of the catalysts of the invention and of the polymerization process using them is the obtainment of polymers having a very low molecular weight, as well as a narrow MWD, which allow to avoid the presence of low soluble fractions in the final polymer.
- the MWD can be varied by using mixtures of different zirconocene compounds, or by carrying out the polymerization in several steps that differ with respect to the temperatures of polymerization and/or the concentrations of molecular weight regulator.
- the polymerization yields depend on the purity of the zirconocene component of the catalyst. Accordingly, the zirconocene compounds obtained by the process of the invention can be used as they are, or they can undergo purification treatments.
- the components of the catalyst can be brought into contact with each other prior to polymerization.
- the duration of contact is generally between 1 and 60 minutes, preferably between 5 and 20 minutes.
- the pre-contact concentrations for the zirconocene component (A) are between 10 ⁇ 2 and 10 ⁇ 8 mol/l, whereas for component (B) they are between 10 and 10 ⁇ 3 mol/l.
- Precontact is generally effected in the presence of a hydrocarbon solvent and, if necessary, of small amounts of monomer.
- Intrinsic viscosities I.V. were measured at 135° C. in tetrahydronaphtalene (THN) or in decalin.
- Mw molecular weight distributions
- Mw/Mn molecular weight distributions
- the triad and dyads distributions, as well as the kinetic parameters r 1 and r 2 were calculated by 13 C-NMR analysis, according to the method described by T. Uozumi and K. Soga ( Macromol. Chem., 193:823, 1992).
- the characterization of the propylene polymers and the determination of the amount of propylene (C3) units in ethylene/propylene copolymers were carried out on a Brucker 500 spectrometer, operating at 125.4 MHz. The samples were dissolved in 1,2,4-trichlorobenzene with some 1,4-dichloro-deuterohexene (1,4-C 6 D 4 Cl 2 ) added as lock.
- the toluene solution was separated by centrifugation and the remaining solid was extracted with 3 ⁇ 25 ml toluene.
- the toluene extracts were combined, concentrated and crystallized at ⁇ 35° C., thus giving 300 mg of rac-1,2-ethylene-bis(1-methyl-2-indenyl)zirconium dichloride.
- the toluene-insoluble precipitate obtained from the reaction mixture was extracted with CH 2 Cl 2 ; CH 2 Cl 2 was removed in vacuum, thus giving a yellow powder. This was washed with 2 ⁇ 5 ml pentane to afford 230 mg of pure meso-1,2-ethylene-bis(1-methyl-2-indenyl)zirconium dichloride.
- 1,2-Bis(1-methyl-2-indenyl)ethane (9.7 g, 33.9 mmol), obtained as described above, was suspended in 100 mL THF and to the obtained mixture were added 28.5 mL n-BuLi (in the form of a 2.5M hexane solution), over a period of 10 minutes, at 0° C.
- the reaction mixture was allowed to warm to 20° C. and maintained under stirring for 90 minutes, at 20° C.; to the thus obtained red/brown solution, previously cooled to 0° C., were added, over few minutes, 5.3 mL MeI in 50 mL THF (also previously cooled to 0° C.). The reaction mixture was allowed to warm to 20° C.
- This ligand was prepared through the intermediate 2,5-bis(2-phenyl-benzyl) adipic acid diethylester, synthesized according to the following reaction scheme:
- the dianion was obtained in the form of a sticky product; after washing with hexane, the orange powder was suspended in 10 mL toluene and 0.29 g of ZrCl 4 were added, at ⁇ 30° C. The reaction mixture was allowed to warm to 20° C. and was stirred overnight. The thus obtained orange suspension was filtered and the filtrate was concentrated and used for crystallization.
- the crude product was 1,2-ethylene-bis(1-methyl4-phenyl-2-indenyl)zirconium dichloride, as a mixture of rac/meso isomers in a 1:1 ratio. By successive crystallizations, it could be obtained as a 4:1 rac/meso mixture. Crystallization from dichloromethane/hexane mixture gave 94% pure meso-isomer.
- This zirconocene was prepared as described in the European patent application EP 0 575 875 (stages (a) and (b) of the synthesis of ethylene-bis(4,5,6,7-tetrahydroindenyl) zirconium dichloride).
- the thus obtained catalyst solution was introduced into the autoclave under an ethylene flow. Then the temperature was brought to 80° C. and kept constant for the duration of the polymerization. The autoclave was pressurized to 4.6 bar and the total pressure was kept constant by feeding ethylene. After the time indicated in Table 1 the polymerization was interrupted by cooling to room temperature, degassing the reactor and introducing 1 ml of methanol. The thus obtained polymer was washed with acidic methanol, then with methanol and dried in oven at 60° C. under vacuum.
- the bridged zirconocene compounds and the catalysts containing them according to the present invention are unexpectedly much more active than the ones known in the state of the art (in particular having bridged bis(1-indenyl) ligands), independently on the cocatalyst used. Furthermore, the gist of the present invention is the possibility of obtaining ethylene homopolymers having low Mw values (endowed with I.V. ⁇ 0.7), unexpectedly much lower than the ones obtainable with the metallocene/alumoxane catalyst systems known in the art.
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Abstract
Zirconocene compounds with two indenyl ligands linked in the 2 position by means of a two-carbon-atoms divalent bridging group can be suitably used as components of catalysts for the polymerization of olefins. Particularly it is possible to prepare, with high yields, ethylene (co)polymers having low molecular weights and narrow molecular weight distributions, without the need of using considerable amounts of molecular weight regulators, such as hydrogen.
Description
- The present invention relates to bridged zirconocene compounds, to the corresponding ligands, to a new process for their preparation and to the use of said zirconocenes as catalytic components in the polymerization of olefins.
- Stereorigid chiral metallocene compounds possessing two bridged indenyl groups are well known in the state of the art and are mainly used as catalytic components in olefin polymerization processes, and in particular in the preparation of stereoregular polyolefins. The numbering of the substituents on the indenyl group, to which reference is made in the present application, in accordance with the IUPAC nomenclature, is the following:
- In the bridged indenyl metallocene compounds known in the state of the art, the indenyl groups are linked together by divalent radicals containing one or more carbon atoms and/or heteroatoms; the divalent bridging groups are generally linked to the 1 position of said indenyl groups, and therefore, the common indenyl metallocenes are 1-indenyl compounds. For example, the European patent application EP 0 485 823 describes a class of bridged bis(1-indenyl) metallocenes, wherein the indenyl groups have a substituent other than hydrogen in the 2 position and are bridged in the 1 position by means of a bridge containing 1 or more carbon atoms (e.g. an ethylene or isopropylidene group) or containing heteroatoms (e.g. a dimethyl-silyl or a diphenyl-silyl group).
- The European patent application EP 0 372 414 describes a very broad class of bridged or unbridged metallocenes; among the many metallocenes exemplified, are reported two specific bis-indenyl metallocene compounds, wherein the divalent group bridging the indenyl groups is linked to the 1 position of one indenyl group and to the 2 position of the other indenyl group (formulae II-1 and II-2, on page 5 of said patent application).
- The International patent application WO 94/11406 describes a very broad class of metallocene compounds of formula R′Ind-M-(CP)Qk, wherein: Ind is an indenyl group; R′ is a substituent, other than hydrogen, linked in the 2 position of said indenyl group; Cp is a cyclopentadienyl group; M is a transition metal belonging to group 3, 4, 5 or 6 of the Periodic Table of Elements; and Q is a σ-ligand of the metal M, k being an integer linked to the valence of said metal M. Among the huge plethora of embodiments envisaged in the reported general formula, R′ can form a bridge between the 2 position of the Ind group and the Cp group of the above formula; therefore, the class of bis(2-indenyl) compounds is generically described. The definition of the bridging group R′ is very broad too, the preferred bridges linking the two indenyl residues being —S—, (CH3)2Si< and —CH2— groups; in fact, in the working examples only bis-indenyl zirconocenes with a one-atom-bridge have actually been synthesized and tested in ethylene (co)polymerization, giving ethylene homopolymers in very low yield and ethylene/propylene copolymers having very low molecular weights and in low yields too.
- The Applicant has now unexpectedly found a new class of bridged bis(2-indenyl)zirconocenes, particularly active as catalyst components for the polymerization of olefins. Said zirconocene compounds are characterized by the presence of two indenyl ligands, bridged in the 2 position by means of a two-carbon-atoms divalent group.
-
- wherein R1, R2, R3 and R4, the same or different from each other, are selected from the group consisting of hydrogen, linear or branched, saturated or unsaturated, C1-C20 alkyl, C3-C20 cycloalkyl, C6-C20 aryl, C7-C20 alkylaryl and C7-C20 arylalkyl radicals, optionally containing one or more Si or Ge atoms, or wherein two substituents of R1, R2, R3 and R4 form a ring having from 4 to 8 carbon atoms;
- R5 and R6, the same or different from each other, are selected from the group consisting of linear or branched, saturated or unsaturated C1-C20 alkyl, C3-C20 cycloalkyl, C6-C20 aryl, C7-C20 alkylaryl and C7-C20 arylalkyl radicals, optionally containing one or more Si or Ge atoms, or two vicinal R6 substituents on the same indenyl group form a ring having from 4 to 8 carbon atoms;
- m is an integer ranging from 0 to 2; n is an integer ranging from 0 to 4;
- the groups X, the same or different from each other, are hydrogen, halogen, —R, —OR, —SR, —NR2 or —PR2, wherein R is selected from the group consisting of linear or branched, saturated or unsaturated, C1-C20 alkyl, C3-C20 cycloalkyl, C6-C20 aryl, C7-C20 alkylaryl and C7-C20 arylalkyl radicals, optionally containing one or more Si or Ge atoms.
- Another object of the present invention is a catalyst for the polymerization of olefins comprising the product obtainable by contacting:
- (A) one or more bridged zirconocene compounds of formula (I), as described above, and
- (B) a suitable activating cocatalyst.
- Furthermore, the present invention provides a process for the polymerization of olefins comprising the polymerization reaction of one or more olefinic monomers in the presence of a catalyst as described above.
-
- wherein R1, R2, R3, R4, R5 and R6, m and n have the meaning reported above, with the proviso that:
- when R1, R2, R3 and R4 are hydrogen and n is 0, then m is different from 0; and
- when R1, R2, R3 and R4 are hydrogen, n is 0 and m is 1, then R5 is different from —CH3, —CH2Ph and —Si(CH3)3.
- The present invention further concerns a process for the preparation of the above ligands of formula (II), comprising the following steps:
- (1) reacting an adipic ester of formula (III) with at least 2 equivalents of a benzyl compound of formula (IV) and at least 2 equivalents of an alkali metal or alkaline earth metal base, in the presence of an organic solvent, to obtain an intermediate compound of formula (V); said step may be represented by the following reaction scheme:
- wherein R1, R2, R3, R4, R6 and n have the meaning reported above, R7 is selected from the group consisting of linear or branched, saturated or unsaturated C1-C20 alkyl, C3-C20 cycloalkyl, C6-C20 aryl, C7-C20 alkylaryl and C7-C20 arylalkyl radicals, and Y is a suitable leaving group;
-
- wherein R1, R2, R3, R4, R6 and n have the meaning reported above and Y′ is a suitable leaving group;
-
- wherein R1, R2, R3, R4, R6 and n have the meaning reported above. When in the ligand of formula (II) m is ≠ 0, then the substituents R5 can be introduced on the cyclopentadienyl ring by reacting a compound of formula (VII) or the same ligand of formula (II) with a suitable amount of an alkylating agent R5MgBr, R5MgCl or R5 jB, wherein B is an alkaline or alkaline-earth metal, and j is 1 or 2.
- Finally, the present invention concerns intermediate compounds of formula (V), as reported above, useful in the synthesis of the ligands (II), according to the present invention.
- The bridged zirconocene compounds of formula (I), the corresponding ligands, the process for their preparation and the catalysts for the polymerization of olefins containing them, according to the present invention, will be better described in the following detailed description.
- It is an object of the present invention a bridged zirconocene compound of formula (I), wherein R1, R2, R3 and R4, the same or different from each other, are selected from the group consisting of hydrogen, linear or branched, saturated or unsaturated, C1-C20 alkyl, C3-C20 cycloalkyl, C6-C20 aryl, C7-C20 alkylaryl and C7-C20 arylalkyl radicals, optionally containing one or more Si or Ge atoms, or wherein two substituents of R1, R2, R3 and R4 form a ring having from 4 to 8 carbon atoms. Preferably R1, R2, R3 and R4 are selected from the group consisting of hydrogen, methyl, ethyl, propyl, phenyl and benzyl; more preferably, R1, R2, R3 and R4 are hydrogen and the bridging group of the two 2-indenyl groups is ethylene.
- In the bridged zirconocene compounds of formula (I), R5 and R6, the same or different from each other, are selected from the group consisting of linear or branched, saturated or unsaturated C1-C20 alkyl, C3-C20 cycloalkyl, C6-C20 aryl, C7-C20 alkylaryl and C7-C20 arylalkyl radicals, optionally containing one or more Si or Ge atoms; or two vicinal R6 substituents on the same indenyl group form a ring having from 4 to 8 carbon atoms. R5 and R6 are preferably selected from the group consisting of methyl, ethyl, propyl, phenyl and benzyl.
- The variable m is an integer ranging from 0 to 2; the variable n is an integer ranging from 0 to 4.
- The groups X, the same or different from each other, are hydrogen, halogen, —R, —OR, —SR, —NR2 or —PR2, wherein R is selected from the group consisting of linear or branched, saturated or unsaturated, C1-C20 alkyl, C3-C20 cycloalkyl, C6-C20 aryl, C7-C20 alkylaryl and C7-C20 arylalkyl radicals, optionally containing one or more Si or Ge atoms. X is preferably Cl, Br or methyl.
- Non-limiting examples of bridged zirconocene compounds according to the present invention are:
- 1,2-ethylene-bis(2-indenyl)zirconium dichloride and dimethyl,
- 1,2-ethylene-bis(1,3-dimethyl-2-indenyl)zirconium dichloride and dimethyl,
- rac- and meso-1,2-ethylene-bis(-methyl-2-indenyl)zirconium dichloride and dimethyl,
- rac- and meso-1,2-ethylene-bis(1-ethyl-2-indenyl)zirconium dichloride and dimethyl,
- rac- and meso-1,2-ethylene-bis(4-phenyl-2-indenyl)zirconium dichloride and dimethyl,
- rac- and meso-1,2-ethylene-bis(1-methyl-4-phenyl-2-indenyl)zirconium dichloride and dimethyl,
- rac- and meso-1,2-ethylene-bis(1-isopropyl-4-phenyl-2-indenyl)zirconium dichloride and dimethyl.
- Said bridged zirconocene compounds can be prepared by reaction of the corresponding ligands of formula (II) first with a compound capable of forming a delocalized anion on the cyclopentadienyl ring, and then with a compound of formula ZrZ4, wherein the substituents Z, the same or different from each other, are halogen (ZrCl4 is particularly preferred), according to common procedures known in the state of the art.
- When, in the zirconocene of formula (I) one or more X groups are other than halogen, it is necessary to substitute one or more halogens Z of the zirconocene dihalide with one or more substituents X other than halogen. The substitution reaction can be carried out by standard procedures, known in the state of the art, for example by reacting the zirconocene dihalide with alkylmagnesium halides (Grignard reagents) or with alkyllithium compounds. It is another object of the invention the ligand of formula (II), wherein R1, R2, R3, R4, R5 and R6, m and n have the meaning reported above, with the proviso that:
- when R1, R2, R3 and R4 are hydrogen and n is 0, then m is different from 0; and
- when R1, R2, R3 and R4 are hydrogen, n is 0 and m is 1, then R5 is different from —CH3, —CH2Ph and —Si(CH3)3.
- In fact, ethylene-bridged bis-2-indenyl ligands, unsubstituted or bearing a substituent —CH3, —CH2Ph or —Si(CH3)3 have been disclosed by Nantz M. H. et al. in Organometallics 1993, 12:5012-5015 and by Hitchcock S. R. et al. in Organometallics 1995, 14:3732-3740. These ligands were used to prepare the corresponding titanocene dichloride, useful in the catalytic epoxidation of unfunctionalized alkenes. The ligands mentioned above are expressly excluded from the ligands according to the present invention.
- The ligands of formula (II), according to the present invention, are prepared by means of a very simple and efficient process, which employs cheap starting materials and comprises single reaction steps having very high yields, some of them almost quantitative. Furthermore, said process does not require laborious and time-consuming purification procedures, being particularly suitable to large scale production.
- The process step (1) comprises reacting the adipic ester of formula (III) with at least 2 equivalents, and preferably 2-4 equivalents of a benzyl compound of formula (IV) and at least 2 equivalents, and preferably 24 equivalents of an alkali metal or alkaline earth metal base, according to the reaction scheme reported in the summary of the invention, to obtain an intermediate compound of formula (V).
- Said reaction is preferably carried out one pot, by sequential addition of said base and of the benzyl compound of formula (IV), in the presence of an organic solvent, at a temperature preferably ranging from 20 to 80° C., and more preferably from 50 to 70° C.
- Said base of an alkali metal or alkaline earth metal is preferably selected from the group consisting of NaOEt, KOEt, KOH, NaOH, NaH, KH and mixtures thereof.
- Said organic solvent is preferably selected from the group consisting of THF, glyme, toluene and mixtures thereof.
- In said compound of formula (IV), Y is preferably Cl or Br.
- Reaction step (2) comprises cycling the compound of formula (V), according to the reaction scheme reported in the summary of the invention, to obtain a compound of formula (VII). According to a preferred embodiment of the process of the invention, said step is conducted first de-esterifying the functions —COOR7 of the compound of formula (V) to the corresponding —COOH groups, by adding at least 2 equivalents, and preferably 2-3 equivalents, of a base in a mixture of aqueous and organic solvent.
- Said base is preferably KOH and/or NaOH. Said mixture of solvents is preferably a mixture of MeOH and water.
- The present reaction step is preferably carried out at a temperature ranging from 20 to 150° C., and more preferably from 70 to 100° C., for a time of 1-5 hours, and more preferably for 2-3 hours.
- The obtained diacid can be isolated by acidification, according to procedures known in the state of the art, and is subsequently derivatized with a suitable leaving group Y′, to give a compound of formula (VI). Said group Y′ is preferably Cl or Br.
- When Y′ is Cl, the compound of formula (VI) can be obtained from the above mentioned diacid by reaction with SOCl2 in excess, and preferably in amounts ranging from 6 to 10 equivalents per leaving group Y′, at a temperature preferably ranging from 20 to 80° C., and more preferably from 50 to 60° C., for a period preferably of 4-12 hours, and more preferably of 7-9 hours.
- The compound of formula (VI) is then cycled to give the final compound (VII), in the presence of at least 1 equivalent of a Lewis acid, and preferably 1.1-1.3 equivalents of AlCl3, at a temperature preferably ranging from 0 and 40° C., in the presence of an organic solvent. The compound (VII) can be finally isolated from the reaction mixture according to standard procedures.
- Reaction step (3) comprises reducing the ketonic functions on the indanyl moieties of the compound of formula (VII) to obtain the diol (VIII) and finally dehydrating the hydroxy functions on the indanyl moieties of said diol (VIII) to give the ligand (II), according to the reaction scheme reported in the summary of the invention.
- The compound (VII) can be reduced to the diol (VIII) by reaction with at least 0.5 equivalents, and preferably 1-1.2 equivalents, of a suitable reducing agent, in an organic solvent.
- Said reducing agent is preferably selected from the group consisting of NaBH4, LiAlH4, NaH and KH; said organic solvent is preferably MeOH. This reaction is preferably carried out at a temperature ranging from −20° C. to 20° C., for a time of 10-18 hours. The diol (VIII) can be then isolated by acidification, according to procedures known in the state of the art.
- Said diol (VIII) is subsequently dehydrated to the ligand (II) by acid treatment or by thermolysis; in the former case, the diol (VIII) is preferably treated with catalytic amounts of an acid, more preferably p-toluensulfonic acid or HCl, in an organic solvent such as ether, toluene and CH2Cl2, at a temperature ranging from 20 to 100° C. In the latter case, the diol (VIII) is preferably dehydrated by thermolysis at a temperature ranging from 200 to 300° C., and more preferably from 250 to 270° C., for a period of 1-2 hours. The final ligand (II) can be then isolated according to standard procedures known in the state of the art. When in the ligand of formula (II) m is ≠ 0, then the substituents R5 can be introduced on the cyclopentadienyl ring by reacting a compound of formula (VII) or the same ligand of formula (II) with a suitable amount of an alkylating agent R5MgX′ or R5 jB, wherein, X′ is halogen, B is an alkaline or alkaline-earth metal and j is 1 or 2.
- Preferably, the compound of formula (VII) or (II) is reacted with at least 2 equivalents of said alkylating agent, at a temperature ranging from −78° C. to 20° C., for a time of 1-3 hours. The reaction is preferably conducted in an organic solvent selected from the group consisting of THF, Et2O, toluene and mixtures thereof. Said alkylating agent is preferably selected from the group consisting of R5MgBr, R5MgCl, R5Li, R5 2Mg and R5 2Zn. The ligands of formula (II) according to the present invention can be easily transformed into the corresponding zirconocenes by using standard procedures known in the state of the art.
-
- wherein R1, R2, R3, R4, R5, R6, R7 and n have the meaning reported above.
- The bridged zirconocene compounds according to the present invention can be advantageously used as catalytic components for the polymerization of olefins. Therefore, another object of the present invention is a catalyst for the polymerization of olefins, comprising the product obtainable by contacting the following components:
- (A) one or more bridged zirconocene compounds of formula (I), as described above, and
- (B) a suitable activating cocatalyst.
-
- wherein the substituents R8, the same or different from each other, are linear or branched, saturated or unsaturated C1-C20 alkyl, C3-C20 cycloalkyl, C6-C20 aryl, C7-C20 alkylaryl, C7-C20 arylalkyl radicals, or groups —O—Al(R8)2.
- Examples of alumoxanes suitable as activating cocatalysts in the catalysts according to the present invention are methylalumoxane (MAO), tetra-isobutyl-alumoxane (TIBAO), tetra-2,4,4-trimethylpentylalumoxane (TIOAO) and tetra-2-methyl-pentylalumoxane. Mixtures of different alumoxanes can also be used.
- Activating cocatalysts suitable as component (B) in the catalysts of the invention are also the products of the reaction between water and organometallic aluminum compounds, preferably of formula AlR8 3 or Al2R8 6, wherein R8 has the meaning reported above.
- Particularly suitable are the organometallic aluminum compounds of formula (II) described in EP-A-575,875 and those of formula (II) described in WO 96/02580. Non-limiting examples of organometallic aluminum compounds of formula AlR8 3 or Al2R8 6 are:
- tris(methyl)aluminum, tris(isobutyl)aluminum, tris(isooctyl)aluminum bis(isobutyl)aluminum hydride, methyl-bis(isobutyl)aluminum, dimethyl(isobutyl)aluminum, tris(isohexyl)aluminum, tris(benzyl)aluminum, tris(tolyl)aluminum, tris(2,4,4-trimethylpentyl)aluminum, bis(2,4,4-trimethylpentyl)aluminum hydride, isobutyl-bis(2-phenyl-propyl)aluminum, diisobutyl-(2-phenyl-propyl)aluminum, isobutyl-bis(2,4,4-trimethyl-pentyl)aluminum and diisobutyl-(2,4,4-trimethyl-pentyl)aluminum.
- Particularly preferred aluminum compounds are tris(2,4,4-trimethylpentyl)aluminum (TIOA), and triisobutylaluminum (TIBA).
- Mixtures of different organometallic aluminum compounds and/or alumoxanes can also be used.
- The molar ratio between aluminum and the metal of the zirconocene is preferably comprised between about 10:1 and about 50,000:1, and preferably between about 100:1 and about 4,000:1.
- Further activating cocatalysts suitable as component (B) in the catalysts of the invention are those compounds capable of forming an alkyl zirconocene cation. Non-limiting examples of these compounds are those of formula Y+Z−, wherein Y+ is a Bronsted acid capable of donating a proton and of reacting irreversibly with a substituent X of the compound of formula (I), and Z− is a compatible anion which does not coordinate, which is capable of stabilizing the active catalytic species originating from the reaction of the two compounds, and which is sufficiently labile to be able to be displaced from an olefinic substrate. The Z− anion preferably comprises one or more boron atoms.
- More preferably, the Z− anion is an anion of formula BAr4 (−), wherein the Ar substituents, the same or different from each other, are aryl radicals such as phenyl, pentafluorophenyl, bis(trifluoromethyl)phenyl. Tetrakis-pentafluorophenyl-borate is particularly preferred. Moreover, compounds of formula BAr3 can be used conveniently.
- The catalysts of the present invention can also be used on inert supports. This is achieved by depositing the zirconocene compound (A), or the product of its reaction with the activating cocatalyst (B), or component (B) and then the zirconocene compound (A), on inert supports such as silica, alumina or olefin polymers or prepolymer such as polyethylenes, polypropylenes or styrene-divinylbenzene copolymers. The thus obtained solid compounds, in combination with further addition of alkyl aluminum compound either untreated or pre-reacted with water, if necessary, is used advantageously in gas-phase polymerization.
- The present invention also provides a process for the polymerization of olefins comprising the reaction of polymerization of one or more olefinic monomers in the presence of a catalyst as described above. Representative examples of olefinic monomers which may be used in the polymerization process of the invention are ethylene, α-olefins such as propylene and 1-butene, cycloolefins and conjugated diolefins.
- The catalysts of the invention can be advantageously used in ethylene homopolymerization or in the copolymerization of ethylene with propylene, 1-butene, 1-hexene, 4-methyl-1-pentene or 1-octene. Said catalysts unexpectedly allow to obtain, in high yields, ethylene polymers having very low molecular weights and having narrow molecular weight distributions (MWDs), without the need of using substantial amounts of molecular weight regulators, such as hydrogen. In particular, with the catalysts of the invention it is possible to obtain, with high yields and without the use of molecular weight regulators, ethylene homopolymers or ethylene/α-olefin copolymers having intrinsic viscosities (I.V.) lower than 1.0 dl/g, preferably comprised between 0.2 and 0.8 dl/g, more preferably between 0.3 and 0.7 dl/g; furthermore, the obtained polymers have a molecular weight distribution MWD (Mw/Mn) lower than 3.
- The catalysts of the invention not always show satisfactory activities in the homopolymerization of propylene to give atactic propylene oligomers. However, when the homopolymerization of propylene is performed in the presence of hydrogen, a very large increase in the activities is unexpectedly observed.
- Therefore, according to another particular embodiment, the present invention provides a process for propylene homopolymerization, carried out in the presence of controlled amounts of hydrogen, which lead to a significant 100-500 fold increase in homopolymerization activity. The amount of hydrogen is preferably comprised between 1 mol % and 30 mol %, with respect to the total quantity of hydrogen and propylene, at the temperature of 50° C.; said amount of hydrogen is more preferably 2-3 mol % of a total amount of hydrogen and propylene.
- The polymerization process according to the present invention can be carried out in the liquid phase, in the presence or absence of an inert hydrocarbon solvent, or in the gas phase. The hydrocarbon solvent can be either aromatic, such as toluene, or aliphatic, such as propane, hexane, heptane, isobutane and cyclohexane.
- The polymerization temperature is generally comprised between −100° C. and +250° C., and more particularly between −50° C. and +100° C. The lower is the polymerization temperature, the higher are the molecular weights of the polymers obtained.
- The molecular weight of the polymers can be further varied by changing the type or the concentration of the catalytic components or by using molecular weight regulators, for example hydrogen. Nevertheless, we stress again that the gist of the catalysts of the invention and of the polymerization process using them is the obtainment of polymers having a very low molecular weight, as well as a narrow MWD, which allow to avoid the presence of low soluble fractions in the final polymer.
- The MWD can be varied by using mixtures of different zirconocene compounds, or by carrying out the polymerization in several steps that differ with respect to the temperatures of polymerization and/or the concentrations of molecular weight regulator.
- The polymerization yields depend on the purity of the zirconocene component of the catalyst. Accordingly, the zirconocene compounds obtained by the process of the invention can be used as they are, or they can undergo purification treatments.
- The components of the catalyst can be brought into contact with each other prior to polymerization. The duration of contact is generally between 1 and 60 minutes, preferably between 5 and 20 minutes. The pre-contact concentrations for the zirconocene component (A) are between 10−2 and 10−8 mol/l, whereas for component (B) they are between 10 and 10−3 mol/l. Precontact is generally effected in the presence of a hydrocarbon solvent and, if necessary, of small amounts of monomer.
- The following experimental examples are given for illustrative and not limiting purposes.
- All the operations with the catalytic systems, the metallocenes and the aluminum alkyls were carried out under nitrogen atmosphere.
- The zirconocenes and their intermediates were characterized by the following methods:
- The1H-NMR and 13C-NMR spectra were recorded in CD2Cl2 (referenced against the middle peak of the triplet of residual CHDCl2 at 5.35 ppm) and C6D6 (referenced against residual C6D5H at 7.15 ppm), using a Varian Gemini 300 (1H NMR at 300 MHz, 13C NMR at 75.4 MHz) or a Varian XL 200 (1H NMR at 200 MHz, 13C NMR at 50.1 MHz). All NMR solvents were dried over 4 Å molecular sieves before use. Preparation of the samples was carried out under nitrogen, using standard inert atmosphere techniques; the measurements were performed at 20° C.
- All the polymerization solvents were used after drying over molecular sieves and deoxygenated; ethylene was used as polymerization grade reagent; 1-hexene was dried over alumina and distilled over LiAlH4. The polymers were characterized by the following methods:
- Intrinsic viscosities I.V. were measured at 135° C. in tetrahydronaphtalene (THN) or in decalin.
- Calorimetric measurements were performed by using a differential scanning calorimeter Perkin Elmer DSC-7. The instrument was calibrated with indium and tin standards. Weighted sample (5-10 mg) was sealed into aluminum pans, heated to 200° C. and kept at that temperature for a time enough (5 minutes) to allow a complete melting of all the crystallites. Successively, after slow cooling at 20° C./min to 0° C., the peak temperature was assumed as crystallization temperature (Tc). After standing 5 minutes at 0° C., the sample was heated to 200° C. at a rate of 10° C./min. In this second eating run, the peak temperature was assumed as melting temperature (Tm) and the area as global melting enthalpy (ΔHf).
- Molecular weights (Mw) and molecular weight distributions (Mw/Mn) were determined by SEC analysis performed by using a “WATERS 200” GPC instrument, working at 135° C. in 1,2-dichlorobenzene stabilized with BHT (2,6-di-t-butyl-4-methyl-phenol) 0.1 wt %.
- The amounts of 1-hexene (C6) units in the ethylene/1-hexene copolymers were determined at 120° C. by a Brucker AC-200 spectrometer operating at 200.13 MHz in the Fourier Transform mode. The powder polymer samples were dissolved in 1,1,2,2-tetrachloro-1,2-dideuteroethane (C2D2Cl4) to give an 8% w/v. concentration. Peak assignments and composition calculations were made according to the method described by H. C. Cheng et al. in Polymer. Bull. (vol.26, page 325, 1991). The triad and dyads distributions, as well as the kinetic parameters r1 and r2 were calculated by 13C-NMR analysis, according to the method described by T. Uozumi and K. Soga (Macromol. Chem., 193:823, 1992). The characterization of the propylene polymers and the determination of the amount of propylene (C3) units in ethylene/propylene copolymers were carried out on a Brucker 500 spectrometer, operating at 125.4 MHz. The samples were dissolved in 1,2,4-trichlorobenzene with some 1,4-dichloro-deuterohexene (1,4-C6D4Cl2) added as lock. The measurements were done in 5 mm NMR tubes at 130° C., with a 70° pulse and a relaxation delay of 15 seconds. The characterization of ethylene/propylene copolymers was made according to the method described by Y. Doi et al. in Makromol. Chem. Rapid Comm. (vol.4, page 169, 1983).
- Methylalumoxane (MAO)
- A commercial (Witco, MW 1400) 10% w/w toluene solution of MAO was dried in vacuum, at 60° C., to obtain a white free-flowing powder. Said powder was solubilized in toluene (1M solution) before use.
- Tris(2,4,4-trimethyl-pentyl)aluminum (TIOA)
- The product commercially available from WITCO was used diluted to a 1 M solution in heptane.
- Tris(2-methyl-propyl)aluminium (TIBAL)
- The commercial product was purchased from Witco and used as a 1M solution in hexane.
- 1,2-ETHYLENE-BIS(2-INDENYL)ZIRCONIUM DICHLORIDE
- (a) Preparation of the ligand 1,2-bis(2-indenyl)ethane
-
- 487 g of NaOEt (6.87 mol, 1.2 equivalents) were suspended in 3.54 kg of THF, in a 10 L cylindrical double-walled glass reactor, equipped with overhead stirrer and oil heating/cooling bath. The obtained suspension was heated to 60° C. and 1170 g (5.73 mol) of diethyl adipate were added, over a period of 1 hour.
- The reaction mixture was stirred for 16 hours, at 60° C., and 820 g (6.41 moles, 1.12 equivalents) of benzyl chloride were added, over a period of 3.75 hours. The resulting product, the diethyl ester of 2-benzyl adipic acid, was maintained under stirring for other 3.5 hours, at 60° C., and the mixture was then allowed to cool to room temperature. 487 g (6.87 moles, 1.2 equivalents) of NaOEt were added to the mixture, over a period of 2 hours, at 23° C., and the reaction was then slowly warmed to 60° C., for 4 hours, and finally stirred for 16 hours at 60° C.
- To the thus obtained mixture were then added 879 g (6.87 moles, 1.2 equivalents) of benzyl chloride, over a period of 1.75 hours. The reaction mixture was stirred at 65° C. for 6 hours and then cooled to 30° C.; an additional 100 g (1.47 moles) of NaOEt were added and, after 5 hours at 60° C., further 207 g (1.62 moles) of benzyl chloride were added, over a period of 1.75 hours, in order to convert the unreacted NaOEt into PhCH2OEt. After 2 hours at 60° C., to the obtained mixture were added 224 g (4.87 moles, 0.85 equivalents) of EtOH and the reaction mixture was allowed to cool to 25° C. After the addition of 2,800 ml dilute HCl (pH 2), 1.43 kg toluene were added and the organic and aqueous layers were separated. The solvents were removed on a rotary evaporator and the higher boiling fractions (namely the excess of benzyl chloride and benzyl ether) were removed on a Schlenk line, at 100° C.
- This purification procedure gave 2,035 g of dibenzyl adipate, having a purity of 95% (92% yield).
-
-
- In a 3 L 3-neck round bottom flask, equipped with an overhead stirrer, were added 723 g (1.89 moles) of diethyl ester of 2,5-dibenzyl-adipic acid, obtained as described above, and 910 ml (5.67 moles) of Claisen alkali solution (a 6.25M solution of KOH in a 1:3/H20:MeOH (v/v) mixture) and the obtained mixture was heated to 90° C. After 3 hours, the reaction mixture was cooled and transferred to a 2 L flask, and the MeOH was removed on a rotary evaporator. The mixture was then washed with 800 mL ether, in order to remove organic impurities, and the obtained viscous water solution was poured into a 5 L beaker, diluted with 1 L water and cooled using an ice bath, to a temperature of about 10° C. To the solution, maintained under constant stirring, was slowly added concentrated HCl, always maintaining the temperature at about 10-15° C.
- At a pH value of about 3, a copious white/beige powdery precipitate formed; concentrated HCl was added until a pH of 1 to 2 was reached, obtaining a final solution of about 4 L. The white precipitate was isolated by filtration and washed with 300 ml water, thus obtaining 2,5-dibenzyl-adipic acid, as a white powder. After drying in a vacuum oven (at 200 mmHg, under nitrogen stream, at 70° C. to remove residual water) to constant weight, 598 g of pure 2,5-dibenzyl-adipic acid were isolated (yield 97% wt.),
-
-
- In a 2 L pear-shaped flask, were added 598 g (1.833 moles) of the 2,5-dibenzyl-adipic acid, prepared as described above, and 2,050 ml of SOCl2 (17.22 mol, density=1.63 g/mL). The obtained mixture was stirred for 16 hours at 20° C., and then heated at 55° C. for 7 hours, thus giving a homogeneous solution; a rapid but controlled gas evolution was observed. After removal of SOCl2 in excess, under vacuum at a bath temperature of 60° C., 300 mL toluene were first added and subsequently removed under vacuum, at 50° C., in order to remove any residual SOCl2. A viscous light brown oil was isolated, which proved to be 2,5-dibenzyl-adipic acid dichloride (two diastereisomers were obtained).
-
-
- In a 3 L 3-neck flask, equipped with a large dropping funnel and kept under nitrogen, 605 g (4.53 moles; 24% excess) of AlCl3 (99%, from Aldrich) were suspended in 800 mL of CH2Cl2, previously dried over molecular sieves; to the obtained suspension was slowly added, over a period of 3 hours, the 2,5-dibenzyl-adipic acid dichloride, prepared as described above, previously dissolved in 1200 ml of CH2Cl2. After stirring for 16 hours at 20° C., venting away the formed HCl, an orange suspension was obtained. This was carefully poured into a water/ice mixture, in a 5 L beaker, and the yellow CH2Cl2 layer was separated; the aqueous phase was extracted with 4×250 ml of CH2Cl2. The CH2Cl2 fractions were collected together and dried with anhydrous MgSO4, thus obtaining a clear red-orange solution. Said solution was filtered and the solvent removed in vacuum, to afford a slightly sticky white solid. After washing with 500 ml pentane, 598 g of the bis(indanone) were isolated in the form of a white powder (yield of 93% wt. from 2,5-dibenzyl-adipic acid).
-
-
- In a 5 L beaker, 494 g (1.70 moles) of the bis(indanone) prepared as described above were suspended in 3 L of THF and 1 L MeOH. After cooling the obtained mixture to about 10° C., with an ice bath, 71 g (1.87 moles) of NaBH4 were slowly added, over a period of 3 hours, maintaining the suspension under vigorous stirring. The addition of NaBH4 resulted in immediate gas evolution. The reaction mixture was maintained under stirring for 16 hours, at 20° C., and then THF and MeOH were removed on a rotary evaporator, thus giving a thick beige slurry. 2 L of water were added to said slurry and the obtained mixture was acidified with dilute HCl till a pH value of 3; a beige powder precipitated and was isolated by filtration. Said powder was extensively washed with water and finally dried to constant weight in a vacuum oven, at 75° C., finally obtaining 506 g of diol.
-
- Dehydration of the diol to give 1,2-bis(2-indenyl)ethane
- 300 g of the diol, prepared as described above, were placed in a 1 L 3 neck round-bottom flask, in a heating mantel; this was heated to a temperature of about 260° C., under nitrogen stream to remove water. The diol melted at about 190° C. The thermolysis was stopped after about 2 hours, thus obtaining a product in the form of a “melted glass”; to this product were added 500 ml of CH2Cl2, by stirring and scratching in order to solubilize said melted glass. The resulting mixture was filtered through a frit, thus isolating the insoluble product, that resulted to be 1,2-bis(2-indenyl)ethane. After washing with pentane, 33.7 g of 1,2-bis(2-indenyl)ethane with a purity of 98.95% (GLC analysis) were isolated, in the form of a white powder.
- CH2Cl2 was removed under vacuum from the CH2Cl2-soluble fraction, to give a slightly oily orange powder. Said powder was washed with pentane to give 74.4 g of 1,2-bis(2-indenyl)ethane in the form of a 96% pure light beige powder. Totally were isolated 108.1 g of the desired ligand 1,2-bis(2-indenyl)ethane, with a 42% yield.
-
- (b) Preparation of the zirconocene dichloride
- In a 2 L 3-necks round bottom flask, under nitrogen stream, to 146 g (0.566 moles) of 1,2-bis(2-indenyl)ethane was added 1 L Et2O and the obtained mixture was cooled to −5° C. by means of a ice/salt bath. To this mixture were slowly added 475 ml of a 2.5 M n-BuLi solution in hexane (2.1 equivalents), over a period of about 2.5 hours. A beige slurry of the dianion was obtained. After having completed the addition, the mixture was stirred for a further 30 minutes, without ice bath, leading to a temperature of 14° C. The volume of the obtained solution was reduced to about 1 L, by removing the solvent under vacuum. This solution was then cooled to −78° C. and added to a suspension of 132 g (0.566 moles) of ZrCl4 in 500 ml of CH2Cl2, in a 2L 3-necks round bottom flask, previously cooled to −78° C. A bright yellow suspension was rapidly obtained. Said suspension was allowed to warm slowly to 20° C. and was stirred for further 16 hours, at 20° C. The solvent was then removed under vacuum, to give a light yellow powder. The pure final product was separated from LiCl and from polymeric byproducts by Soxhlet extraction with CH2Cl2, thus obtaining 197 g of 1,2-ethylene-bis(2-indenyl)zirconium dichloride (yield of 83% wt.).
-
- Elemental analysis: Calculated: C 57.40; H 3.85. Found: C 57.29; H 4.00.
- 1,2-ETHYLENE-BIS(2-INDENYL)ZIRCONIUM DIMETHYL
- 150 mg of 1,2-ethylene-bis(2-indenyl)zirconium dichloride, obtained as described in Synthesis 1, were suspended in 10 ml toluene and cooled to −78° C. 2 equivalents of MeLi we re added and the reaction mixture was allowed to warm to room temperature. The reaction mixture was centrifuged and toluene was removed in vacuum, thus obtaining 80 mg of 1,2-ethylene-bis(2-indenyl)zirconium dimethyl.
-
- Rac- AND meso-1,2-ETHYLENE-BIS(1-METHYL-2-INDENYL) ZIRCONIUM DICHLORIDE
- (a) Preparation of the ligand 1,2-bis(1-methyl-2-indenyl)ethane
- 1.5 g (5.8 mmol) of 1,2-bis(2-indenyl)ethane, prepared as described in the above reported Synthesis 1(a), was dissolved in 25 ml THF and cooled to 0° C. n-BuLi (7.4 ml of a 1.6 M solution in hexane) was added and the resulting orange/brown solution stirred for 1 hour. This was added via a cannula to a solution of MeI (0.9 ml, 14.5 mmol) dissolved in 10 ml THF, at 0° C. After 2 hours, the THF was removed under vacuum and Et2O was added. This Et2O solution was washed 3 times with a saturated solution of NaHCO3 and 3 times with a saturated aqueous solution of NaCl. After drying over MgSO4, 1.4 g of yellow crystalline 1,2-ethylene-bis(1-methyl-2-indenyl)ethane was obtained. The ratio of double bond isomers is ca. 10:1. NMR data are reported for the major double bond isomer, i.e. the rac-isomer.
-
- (b) Preparation of the zirconocene
- 4.1 ml of a solution 2.5 M of n-BuLi in hexane were added to 1.4 g 1,2-ethylene-bis(1-methyl-2-indenyl)ethane, prepared as described above, in 50 ml Et2O cooled to 0° C. After 45 minutes, Et2O was removed in vacuum and the resulting dianion was suspended in 80 ml toluene, at 20° C., in a drybox. 1.15 g (4.93 mmol) of ZrCl4, in the form of a slurry in 10 ml toluene, were added and the reaction mixture changed from yellow to dark brown. After stirring for 21 hours at 20° C., the toluene solution was separated by centrifugation and the remaining solid was extracted with 3×25 ml toluene. The toluene extracts were combined, concentrated and crystallized at −35° C., thus giving 300 mg of rac-1,2-ethylene-bis(1-methyl-2-indenyl)zirconium dichloride. The toluene-insoluble precipitate obtained from the reaction mixture was extracted with CH2Cl2; CH2Cl2 was removed in vacuum, thus giving a yellow powder. This was washed with 2×5 ml pentane to afford 230 mg of pure meso-1,2-ethylene-bis(1-methyl-2-indenyl)zirconium dichloride.
- Rac-isomer:
-
- Elemental analysis: Calculated: C 59.18; H 4.51. Found: C 58.94; H 4.57.
- Meso-isomer:
-
- Rac- AND meso-1,2-ETHYLENE-BIS(1-METHYL-2-INDENYL) ZIRCONIUM DIMETHYL
- 20 mg of rac- and 20 mg of meso-1,2-ethylene-bis(1-methyl-2-indenyl)zirconium dichloride, obtained as described in Synthesis 3, were separately suspended in 1 ml of C6D6, in different NMR tubes. About 5 mg of MeLi in excess, in the form of a white powder, were added to each NMR tube in the drybox. Occasional shaking of the NMR tube gave within 2 hours clean conversion to the corresponding rac- and meso-1,2-ethylene-bis(1-methyl-2-indenyl)zirconium dimethyl isomers.
- Rac-isomer:
-
- Meso-isomer:
-
- Rac- AND meso-1,2-ETHYLENE-BIS(1-ETHYL-2-INDENYL) ZIRCONIUM DICHLORIDE
- (a) Preparation of the ligand 1,2-bis(1-ethyl-2-indenyl)ethane
- 1.36 g, 5.26 mmol of 1,2-bis(2-indenyl)ethane, prepared as described in the above reported Synthesis 1(a), were dissolved in 25 mL THF and cooled to −10° C. 5.5 ml of a 1.6 M solution of BuLi in hexane (8.8 mmoles) were added and the resulting orange/brown solution was stirred for 2 hours, at room temperature. To the obtained mixture was added, by means of a cannula, a solution of 1.1 ml of EtI (7.1 mmol) in 10 ml THF, at −10° C. After 2 hours, the THF was removed under vacuum, and Et2O was added. The thus obtained etcher solution was washed 3 times with a saturated solution of NaHCO3 and 3 times with a saturated aqueous solution of NaCl. After drying over MgSO4, 1.46 g of 1,2-bis(1-ethyl-2-indenyl)ethane was isolated, in the form of a yellow oil. 1H NMR and GC showed that it consisted of the three possible double bond isomers.
- (b) Preparation of the zirconocene
- 4.5 ml of a 1.6 M solution of n-BuLi in hexane (7.2 mmol) were added to a suspension of 1.16 g (3.5 mmoles) of 1,2-bis(1-ethyl-2-indenyl)ethane, obtained as described above, in 50 ml of Et2O, at −10° C. The mixture was maintained under stirring for 45 minutes and Et2O was removed in vacuum; the thus obtained dianion was suspended in 80 ml of toluene, at 20° C. in a drybox. A slurry of 1.16 g (4.93 mmoles) of ZrCl4 in 10 ml of toluene was added to the reaction mixture, which turned from yellow to dark brown. After stirring for 21 hours, at 20° C., the toluene solution was separated by centrifugation and the remaining solid was extracted with toluene (3×25 ml). The toluene extracts were combined, concentrated and crystallized at −35° C., thus giving 72 mg of rac-1,2-ethylene-bis(1-ethyl-2-indenyl)zirconium dichloride.
- The toluene-insoluble precipitate, obtained from the reaction mixture, was extracted with CH2Cl2; after removal of the CH2Cl2 in vacuum, a yellow powder was obtained, which was washed with pentane (2×5 ml) to give 300 mg of pure meso-1,2-ethylene-bis(1-ethyl-2-indenyl)zirconium dichloride.
- Rac-isomer:
-
- Meso-isomer:
-
- Meso-1,2-ETHYLENE-BIS(1-ETHYL-2-INDENYL) ZIRCONIUM DIMETHYL
- 20 mg of meso-1,2-ethylene-bis(1-ethyl-2-indenyl)zirconium dichloride, prepared as described in the above reported Synthesis 5, were suspended in 1 ml of C6D6 in a NMR tube. About 5 mg of MeLi in excess, in the form of a white powder, were added in the drybox. Occasional shaking of the NMR tube gave within 2 hours the final product meso-1,2-ethylene-bis(1-ethyl-2-indenyl)zirconium dimethyl.
-
- 1,2-ETHYLENE-BIS(1,3-DIMETHYL-2-INDENYL) ZIRCONIUM DICHLORIDE
- (a) Preparation of the ligand 1,2-bis(1,3-dimethyl-2-indenyl)ethane
-
- 10 g (38.7 mmoles) of 1,2-bis(2-indenyl)ethane, prepared as described in the above Synthesis 1(a), were suspended in 100 mL THF and to the obtained mixture were added 32 mL n-BuLi (2.5 M solution in hexane), during 15-minutes, at 0° C. The resulting solution was allowed to warm to 20° C. and maintained under stirring for 30 minutes at 20° C.; to the thus obtained red/brown solution, previously cooled to 0° C., were then added, over a few minutes, 6.0 mL MeI in 50 mL THF (also previously cooled to 0° C.). The reaction mixture was allowed to warm to 20° C. and was maintained under stirring for 2 hours. Subsequently, the solvent were removed in vacuum. The thus obtained sticky yellow/orange solid was dissolved in 200 mL Et2O and extracted 3 times with a saturated aqueous solution of NaHCO3 and a saturated solution of NaCl. The aqueous and organic layers were separated and Et2O was removed in vacuum, thus yielding 9.7 g (yield of 88%) of 1,2-bis(1-methyl-2-indenyl)ethane. This product consisted of a mixture of the 3 isomers reported above, wherein the double bond isomeric moieties I and II, reported below, are formed in a ratio of about 1:10 (confirmed by 1H-NMR analysis):
-
- Preparation of 1,2-bis(1,3-dimethyl-2-indenyl)ethane
- 1,2-Bis(1-methyl-2-indenyl)ethane (9.7 g, 33.9 mmol), obtained as described above, was suspended in 100 mL THF and to the obtained mixture were added 28.5 mL n-BuLi (in the form of a 2.5M hexane solution), over a period of 10 minutes, at 0° C. The reaction mixture was allowed to warm to 20° C. and maintained under stirring for 90 minutes, at 20° C.; to the thus obtained red/brown solution, previously cooled to 0° C., were added, over few minutes, 5.3 mL MeI in 50 mL THF (also previously cooled to 0° C.). The reaction mixture was allowed to warm to 20° C. and was-maintained under stirring for 2 hours. After removal of the solvent in vacuum, the thus obtained sticky yellow/orange solid was dissolved in 200 mL Et2O and extracted 3 times with a saturated aqueous solution of NaHCO3 and a saturated aqueous solution of NaCl. The aqueous and organic layers were separated and Et2O was removed in vacuum; the resulting yellow sticky solid was washed with hexane, to give 2.3 g of 1,2-bis(1,3-dimethyl-2-indenyl)ethane (24% yield).
- (b) Preparation of the zirconocene
- Preparation of the dianion of 1,2-bis(1,3-dimethyl-2-indenyl)ethane
- 1.47 g (4.68 mmol) of 1,2-bis(1,3-dimethyl-2-indenyl)ethane were dissolved in 30 mL Et2O and to the obtained solution were added 3.9 mL n-BuLi (as a solution 2.5 M in hexane), at −78° C., over a period of 5 minutes. The reaction mixture was maintained under stirring for 30 minutes, at −78° C., and then was allowed to warm to 20° C. A precipitate formed during the reaction. The thus obtained orange/brown reaction mixture was filtered and the solid was washed with 20 ml hexane, in order to remove 1,1′-dimethylated products, thus giving the dianion of 1,2-bis(1,3-dimethyl-2-indenyl)ethane, in the form of a white/yellow solid, which was used without further purification for the subsequent reaction with ZrCl4, as described below.
-
- Preparation of 1,2-ethylene-bis(1,3-dimethyl-2-indenyl)zirconium dichloride
- The dianion of 1,2-bis(1,3-dimethyl-2-indenyl)ethane, obtained as described above, was suspended in 30 mL toluene and to the obtained mixture was added, at −30° C., over a period of few minutes, a suspension of 0.95 g (4.08 mmol) of ZrCl4 in 10 ml toluene.
- The reaction mixture was allowed to warm to 20° C. and the color changed to orange. The mixture was maintained under stirring overnight and was subsequently filtered; the obtained solid was extracted with toluene (3×10 ml). After removal of the solvent in vacuum, the obtained solid was washed with hexane, to afford 206 mg of 1,2-ethylene-bis(1,3-dimethyl-2-indenyl)zirconium dichloride, as an orange powder.
-
- Rac- AND meso-1,2-ETHYLENE-BIS(4-PHENYL-2-INDENYL) ZIRCONIUM DICHLORIDE
- (a) Preparation of the ligand 1,2-bis(4-phenyl-2-indenyl)ethane
-
- Into a 3 neck flask, equipped with water cooler, were added 43.8 mL (0.22 mol) of diethyladipate and 220 mL THF. 16.3 g (0.24 mol, 1.1 equivalents) of NaOEt were added in small portions, at 20° C., and the reaction mixture was stirred at 60° C. for 16 hours. After cooling to 20° C., 48.6 g (0.20 mol) of 2-phenyl-benzyl bromide was added dropwise. The reaction mixture was stirred at 60° C., for 16 hours, to give 2-(2-phenyl-benzyl) adipic acid diethylester as a viscous oil, in a yield of 92%.
-
- Under the operating conditions reported above, to the obtained diethylester were sequentially added 14.9 g (0.22 mol) of NaOEt and 44.4 g (0.18 mol) of 2-phenyl-benzyl bromide; the obtained mixture was stirred for 16 hours, at 60° C. After the addition of dilute HCl to neutralize the base, the THF and the aqueous acidic phases were separated. The aqueous acidic layer was extracted 3 times with CH2Cl2. The combined THF and CH2Cl2 extracts were evaporated to dryness, to give the intermediate 2,5-bis(2-phenyl-benzyl) adipic acid diethylester, in the form of a very viscous oil.
-
-
-
-
-
-
-
-
-
-
- Isomer 1:
-
- Isomer 2:
-
- (b) Preparation of the zirconocene
- 465 mg, 1.13 mmol of 1,2-bis(4-phenyl-2-indenyl)ethane, prepared as described above, were dissolved in 20 mL Et2O, in a Schlenk tube, and cooled to −78° C. 0.95 mL of n-BuLi as a solution 2.5 M in hexane (2.38 mmol; 2.1 equiv.) was added dropwise. The reaction mixture was allowed to warm to 20° C. Et2O was removed under vacuum, to afford the dianion, in the form of a light-yellow powder.
-
- The above obtained dianion was suspended in toluene and cooled to −20° C.; to the obtained mixture were added 0.28 g (1.19 mmol; 1.05 equivalents) of ZrCl4. The reaction mixture was maintained under stirring for 16 hours, at 20° C.; then it was centrifuged and the toluene layer was discarded. The remaining powder was washed with toluene (20 mL) and then extracted with CH2Cl2, in order to separate the product from LiCl. A pure mixture of rac and meso-isomers of 1,2-ethylene-bis(4-phenyl-2-indenyl)zirconium dichloride was obtained, in the form of a yellow powder. By crystallization from toluene, the meso isomer could be completely separated from the rac-isomer. The rac-isomer was obtained as a rac:meso mixture of about 4:1.
- Rac-isomer:
-
- Meso-isomer:
-
- Meso-1,2-ETHYLENE-BIS(4-PHENYL-2-INDENYL) ZIRCONIUM DIMETHYL
- Meso-1,2-Ethylene-bis(4-phenyl-2-indenyl)zirconium dichloride, obtained as described in the above Synthesis 9, were suspended in C6D6 and MeLi in excess was added; after 30 minutes at 20° C., meso-1,2-ethylene-bis(4-phenyl-2-indenyl)zirconium dimethyl was obtained.
-
- Rac- AND meso-1,2-ETHYLENE-BIS(1-METHYL-4-PHENYL-2-INDENYL) ZIRCONIUM DICHLORIDE
- (a) Preparation of the ligand 1,2-bis(1-methyl-4-phenyl-2-indenyl)ethane
-
- To a solution of 67.8 mL MeMgBr (3M in ether) in 100 mL Et2O was added a solution of 15 g (33.9 mmol) of 1,2-bis(4-phenyl-indanonyl)ethane, prepared as described in the above synthesis 8(a), in 150 mL THF, over a period of 45 minutes, at 0° C. The formation of a white/beige precipitate was observed. The reaction mixture was allowed to warm to 20° C. and was maintained under stirring for 2 hours. The reaction mixture was then poured into ice and acidified to pH 1, with 37% HCl, and finally extracted with Et2O. The organic layer was extracted with a saturated solution of NaCl and the solvent was removed in vacuum. The formed diol was dissolved in CH2Cl2 and p-toluene-sulfonic acid was added. The mixture was stirred overnight at 20° C. The solution was dried over MgSO4, filtered and the solvent was removed in vacuum, thus yielding 9.0 g of the ligand 1,2-bis(1-methyl4-phenyl-2-indenyl)ethane (69% yield).
-
- (b) Preparation of the zirconocene
- To a solution of 0.54 g (1.23 mmol) of 1,2-bis(1-methyl-4-phenyl-2-indenyl)ethane, prepared as described above, in 20 mL Et2O, was added 1.1 mL of n-BuLi (in the form of a 2.5M solution in hexane), at −78° C. The reaction mixture was allowed to warm to 20° C.; the formation of a precipitate was observed and the color changed to orange/red. The reaction mixture was stirred for 2 hours, at 20° C., and the solvent was removed in vacuum. The dianion was obtained in the form of a sticky product; after washing with hexane, the orange powder was suspended in 10 mL toluene and 0.29 g of ZrCl4 were added, at −30° C. The reaction mixture was allowed to warm to 20° C. and was stirred overnight. The thus obtained orange suspension was filtered and the filtrate was concentrated and used for crystallization.
- The crude product was 1,2-ethylene-bis(1-methyl4-phenyl-2-indenyl)zirconium dichloride, as a mixture of rac/meso isomers in a 1:1 ratio. By successive crystallizations, it could be obtained as a 4:1 rac/meso mixture. Crystallization from dichloromethane/hexane mixture gave 94% pure meso-isomer.
- Rac isomer:
-
- Meso isomer:
-
- Rac- AND meso-1,2-ETHYLENE-BIS(1-ISOPROPYL-4-PHENYL-2-INDENYL) ZIRCONIUM DICHLORIDE
- (a) Preparation of the ligand 1,2-bis(1-isopropyl-4-phenyl-2-indenyl)ethane
-
- In a 250 mL flask, containing 40 mL of a solution 2.0 M of i-PrMgCl in Et2O (9 equivalents), previously cooled to 0° C., was added dropwise, over a period of 15-20 minutes, a solution of 4 g of 1,2-bis(4-phenyl-indanonyl)ethane (9.17 mmol), prepared as described in the above synthesis 8(a), in 80 mL THF. The obtained mixture was stirred for 90 minutes and then poured onto ice. The organic layer was separated and the aqueous layer extracted with CH2Cl2. The combined organic layers were washed with a saturated solution of NaCl and then dried over MgSO4, to give the diol. This product was dissolved in 100 ml of CH2Cl2 and to the obtained solution were added 1.5 g of p-toluensulfonic acid; the reaction mixture was maintained under stirring for 20 hours, at 20° C. The obtained mixture was dried with MgSO4, to give a clear yellow solution, which was filtered through a plug of silica to give pure 1,2-bis(1-isopropyl4-phenyl-2-indenyl)ethane.
-
- (b) Preparation of the zirconocene
- 0.29 g (0.58 mmol) of 1,2-bis(1-isopropyl-4-phenyl-2-indenyl)ethane, prepared as described above, were dissolved in 30 mL Et2O and cooled to −78° C. 0.5 mL of n-BuLi (in the form of a 2.5M solution in hexane) were added. The obtained yellow solution became brown-red and the reaction mixture was allowed to warm to 20° C. The reaction mixture was stirred for 1 hour at 20° C. and Et2O was removed in vacuum to give the dianion.
-
- First isomer:
-
- Second isomer:
-
- Rac-1,2-ETHYLENE-BIS(1-INDENYL)ZIRCONIUM DICHLORIDE (EBIZrCl2)
- This zirconocene was prepared as described in the European patent application EP 0 575 875 (stages (a) and (b) of the synthesis of ethylene-bis(4,5,6,7-tetrahydroindenyl) zirconium dichloride).
- METHYLENE-BIS(2-INDENYL)ZIRCONIUM DICHLORIDE
- (a) Preparation of the ligand bis(2-indenyl)methane
- 44.3 g (335 mmol) of 1-indanone, 14.3 g (477 mmol) of paraformaldehyde and 38.4 g (471 mmol) of Me2NH.HCl were combined in 105 ml absolute EtOH and 25 drops of 37% HCl added. This was refluxed for 2.5 hours. After allowing to cool to room temperature, a copious crystalline white precipitate formed. This was filtered off and washed with hexane to give 52.2 g (69%) of the Mannich base 2-CH2N(CH3)2.HCl-1-indanone.
-
- 52.2 g (232 mmol) of the Mannich base, prepared as described above, 43.2 g (327 mmol, 1.4 equivalents) of 1-indanone and 18.2 g (325 mmol, 1.4 equivalents) of KOH were placed in a 250 ml round-bottom flask and 200 ml toluene added. This was brought to reflux whereupon the color changed from yellow to a light purple. After 3 hours reflux, the solution was allowed to cool, more KOH was added and the refluxing continued whereupon the reaction mixture became a dark purple color. This was then allowed to cool to room temperature. This was diluted with ether and washed with saturated aqueous NaHCO3 solution. The layers were separated, the water layer extracted with ether, the ether extracts were combined, and dried over MgSO4. The solvents were evaporated to give a brown oil. This proved to be a mixture of 1-indanone and product. The brown oil was washed with hexane and ether in order to extract 1-indanone. In this way, 15.1 g (24%) of pure CH2(1-indanone)2 were isolated.
-
- 15.0 g (54 mmol) of CH2(1-indanone)2, prepared as described above, and 24.3 g (2.4 equiv.) of tosyl hydrazine were placed in a 250 ml round-bottom flask and 100 ml EtOH added. Then 10 drops of 37% HCl were added and the reaction mixture brought to reflux under nitrogen. On coming to reflux, everything dissolved and a clear brown solution resulted. After refluxing for 10 minutes, a white jelly-like material began to precipitate. This was washed with MeOH and then dried under vacuum. This gave 21 g (63%) of the bis(hydrazone). 10.8 g (17.6 mmol) of the bis(hydrazone), suspended in 250 ml N,N,N′,N′-tetramethyl-ethylene diamine (TMEDA) in a large Schlenk tube, was slowly added to 15.2 g (141 mmol, 8 equivalents) of lithium diisopropylamide, dissolved in 50 ml TMEDA and cooled to 0° C. The solution changed from yellow to purple and then to dark purple. It was allowed to warm to room temperature and then decanted onto ice to give a yellow solution. On washing with 100 ml aqueous NaHCO3 the solution became purple. This was extracted copiously (3×250 ml) with Et2O, the Et2O extracts combined and dried over MgSO4. These were evaporated to a brown oil which was extracted with pentane. Working up of the pentane extracts afforded 0.59 g (14%) of bis(2-indenyl)methane.
-
- (b) Preparation of the zirconocene dichloride
- 0.29 g (1.19 mmol) of bis(2-indenyl)methane, prepared as described above, were dissolved in 40 ml ether and cooled to −78° C. Then 1.6 ml of a 1.6 M solution of n-BuLi in hexane (2.1 equivalents) were added by syringe. It was allowed to warm to room temperature. After 90 minutes at room temperature it was cooled to −78° C. and 0.29 g ZrCl4, suspended in 30 ml Et2O, was added. On allowing to warm to room temperature and stirring for 2 hours, the color changed from brown to yellowish. The solvent was removed under vacuum and the powder washed with Et2O and then hexane to give 300 mg of methylene-bis(2-indenyl)zirconium dichloride as a yellow powder.
-
- Ethylene homopolymerization
- A 200 ml glass autoclave, equipped with magnetic stirrer, temperature indicator and feeding line for the ethylene, was purified and fluxed with ethylene at 35° C. Then 90 ml of n-hexane were charged at room temperature. The catalytic system was prepared by adding to 10 ml of hexane, in the following order, first the aluminum cocatalyst indicated in Table 1, then, in the case of TIOA and TIBAL, water in an amount to give a molar ratio Al/H2O=2.1 and finally, after 5 minutes stirring, the metallocene indicated in Table 1 dissolved in the lowest possible amount of toluene. After further five minutes stirring the thus obtained catalyst solution was introduced into the autoclave under an ethylene flow. Then the temperature was brought to 80° C. and kept constant for the duration of the polymerization. The autoclave was pressurized to 4.6 bar and the total pressure was kept constant by feeding ethylene. After the time indicated in Table 1 the polymerization was interrupted by cooling to room temperature, degassing the reactor and introducing 1 ml of methanol. The thus obtained polymer was washed with acidic methanol, then with methanol and dried in oven at 60° C. under vacuum.
- Polymerization reactions of Examples 3-5 were carried out following the above procedure, with the difference that a 2.3 L reactor and 1 L hexane were used and, during the polymerization, the autoclave was pressurized to 10 bar and the total pressure was kept constant by feeding ethylene. Finally, the polymerization of Example 5 was carried out in the presence of H2 (0.2 bar).
- The polymerization conditions and the characterization data of the obtained polymers are indicated in Table 1.
- From the obtained results, it is evident that the bridged zirconocene compounds and the catalysts containing them according to the present invention are unexpectedly much more active than the ones known in the state of the art (in particular having bridged bis(1-indenyl) ligands), independently on the cocatalyst used. Furthermore, the gist of the present invention is the possibility of obtaining ethylene homopolymers having low Mw values (endowed with I.V.<0.7), unexpectedly much lower than the ones obtainable with the metallocene/alumoxane catalyst systems known in the art.
- Ethylene/1-hexene copolymerization
- The same procedure as that of Examples 1-13 and comparative A-E was followed with the exception that, instead of the hexane, 100 ml of a heptane/1-hexene solution was used (the amounts of 1-hexene are those indicated in Table 2, the rest to 100 ml being heptane) and that the temperature of polymerization was 70° C. When TIOA was used as cocatalyst, water was added in amounts to give a molar ratio Al/H2O=2.1.
- The polymerization conditions and the characterization data of the obtained polymers are indicated in Table 2.
- The reported results demonstrate that the bridged zirconocene compounds and the catalysts containing them according to the present invention allow to obtain polymers having low Mw and narrow MWD values.
- Furthermore, the obtained copolymers showed a completely homogeneous distribution of the comonomer along the polymer chain, as confirmed by the results reported in Table 3.
- Propylene homopolymerization
- 500 molar equivalents of MAO (10% wt. toluene solution) were premixed with the amount of the metallocene indicated in Table 4 and stirred in a drybox at 20° C. for a known time, between 1.5 hours and overnight. Into a 5 L autoclave containing 1.6 Kg propylene, MAO was injected and subsequently (5 minutes later) the premix added. The total Zr:MAO ratio is indicated in Table 4. The reactor was held at 30° C. for 1 minute and then the temperature raised with a temperature gradient of 4° C./minute to 50° C. Polymerization was continued for the time indicated in Table 4 at 50° C. After the time indicated in Table 4 the polymerization was interrupted by rapidly venting the excess of propylene to the incinerator. The thus obtained polymer was isolated according to standard procedures. The polymerization conditions and the characterization data of the obtained polymers are indicated in Table 4.
- Ethylene/propylene copolymerization
- It was worked as in Examples 24-41, with the exception that the polymerization was conducted in a 25 L autoclave containing 7.5 kg propylene and with an ethylene/propylene feed ratio of about 6 mol % (liquid phase). This is equivalent to a 3.3 bar ethylene overpressure. The feed ratio (mol %) of ethylene in the Examples is reported in Table 5. The feed ratio was kept constant throughout the polymerization by adding ethylene on demand. The total amount of MAO added was 11.0 g. The MAO was used as a toluene solution containing 4.84% Al. The reactor temperature was 50° C. Due to effective cooling system, the copolymerizations were essentially isothermal with typical initial exotherms of 1-5° C. being observed (i.e. at maximum cooling capacity, the temperature in the autoclave rose by 1-5° C.). The copolymerization was continued for the time reported in Table 5 and then killed by injection of 2.5 mL MeOH. In several runs the copolymer adhered to the autoclave walls and so was extracted with toluene (140° C.). The toluene was removed on a rotary evaporator and the weight of this fraction added to that was directly removed from the reactor to determine the overall yield and hence activity. This fraction was not used for NMR or LVN analysis. The polymerization conditions and the characterization data of the obtained polymers are indicated in Table 5.
TABLE 1 Ethylene homopolymerization Cocatalyst Metallocene Al/Zr Time Yield Activity I.V.* Example Type mg Type mmol mol/mol (min) (g) (Kg/g · Zrh) (dl/g) Mw · 10-3 Mw/Mn 1 EB(2-Ind)2ZrCl2 0.100 MAO 0.24 1000 10 2.88 528.6 0.42 2 ″ 0.104 TIOA 0.25 1000 10 3.25 860.3 0.54 3 ″ 0.400 TIOA 0.90 1000 60 41 470 0.60 4 ″ 0.200 TIOA 0.10 2000 30 94 2160 0.56 2.6 5 ″ 0.200 TIOA 0.10 2000 60 64 1470 0.47 23 2.6 6 r-EB(1-Me-2-Ind)2ZrCl2 0.100 MAO 0.14 600 10 1.20 352.5 0.47 7 ″ 0.100 TIBAL 0.23 1000 10 3.66 1075 0.59 8 ″ 0.100 MAO 0.23 1000 10 2.75 807.9 0.46 9 ″ 0.100 TIOA 0.22 1000 10 4.61 1354.3 0.67 10 ″ 0.050 TIOA 0.21 1900 10 2.30 1351.3 0.63 32000 2.3 11 m-EB(1-Me-2-Ind)2ZrCl2 0.100 MAO 0.23 1000 10 1.92 564.0 0.36 12 ″ 0.100 TIOA 0.21 1000 10 1.57 461.2 0.37 18000 2.5 13 ″ 0.100 TIBAL 0.23 1000 10 1.28 376.0 0.36 COMP. A CH2(2-Ind)2ZrCl2 0.300 MAO 0.75 1000 10 1.51 132.6 0.17 COMP. B ″ 0.500 MAO 2.50 2000 10 3.39 178.6 0.12 COMP. C ″ 0.500 TIOA 2.50 2000 30 1.54 27.0 0.20 COMP. D EBIZrCl2 0.088 MAO 0.21 1000 10 1.31 409.8 1.38 COMP. E ″ 0.088 TIOA 0.21 1000 10 1.18 369.2 1.60 -
TABLE 2 Ethylene/1-hexene copolymerization Cocatalyst Metallocene TIOA Al/Zr C2H4 C6 Time Yield Activity I.V.* C6 Tm ΔHf Mw Ex. Type mg mmol mol/mol (bar) (ml) (min) (g) (Kg/gZr · h) (dl/g) (% w) (° C.) (J/g) 10-3 Mw/Mn 14 EB(2-Ind)2ZrCl2 0.077 0.18 1000 4.4 0 15 1.65 395.9 0.60 0 132.9 233 — — 15 ″ 0.074 0.18 1000 4.5 5 15 1.70 423.9 0.75 1.5 127.2 213 — — 16 ″ 0.083 0.20 1000 4.5 5 15 2.25 497.5 0.54 1.7 124.2 188 — — 17 ″ 0.074 0.18 1000 4.5 10 15 2.62 653.4 0.60 2.9 120.9 162 — — 18 ″ 0.083 0.20 1000 4.4 15 15 3.18 703.2 0.57 4.0 118.4 152 — — 19 ″ 0.100 0.24 1000 4.2 50 30 3.88 356.1 0.49 9.9 116.0 86 22 2.6 20 r-EB(1-Me-2-Ind)2ZrCl2 0.050 0.12 1000 4.4 15 20 3.72 1092.8 0.59 5.4 116.7 154 — — 21 ″ 0.050 0.11 1000 4.2 50 30 5.60 1096.7 0.58 16.4 95.3 90 33 2.2 22 m-EB(1-Me-2-Ind)2ZrCl2 0.100 0.23 1000 4.4 15 20 3.20 470.0 0.30 9.9 108.9 139 18 2.3 23 ″ 0.200 0.45 1000 4.2 50 30 6.46 316.3 0.33 31.2 amorphous — — -
TABLE 3 Parameter Unit Example 18 Example 19 Triad distribution EEE mol % 95.73 89.42 HEE mol % 2.90 7.05 HEH mol % 0.00 0.00 EHE mol % 1.37 3.53 HHE mol % 0.00 0.00 HHH mol % 0.00 0.00 Dyad distribution EE mol % 97.2 92.9 EH mol % 2.80 7.1 HH mol % 0.00 0.00 Calculated parameters n(E) 70.4 27.1 r1 182 235 r2 0 0 -
TABLE 4 Propylene homopolymerizaion Metallocene Al/Zr H2 Time Yield Activity I.V.* NMR Ex. Type μmol mol/mol (mol %) (min) (g) (Kg/gZr · h) (dl/g) Mn 2,1(%) 24 EB(2-Ind)2ZrCl2 4.0 1000 0 61 0.7 1.9 0.36 1700 9.4 25 ″ 2.0 10000 2-3 60 97 530 — 500 26 r-EB(1-Me-2-Ind)2ZrCl2 3.75 5400 0 60 5.5 16 0.25 2700 2.7 27 ″ 4.0 5000 2-3 5 277 9100 — 1100 28 ″ 0.5 40200 2-3 60 284 6240 — 850 29 m-EB(1-Me-2-Ind)2ZrCl2 4.0 5000 0 60 5.4 15 — 3600 0.4 30 EB(1,3-diMe-2-Ind)2ZrCl2 4.0 5000 0 60 22 60 — 5500 0.2 31 ″ 0.5 40000 2.7 60 230 5030 — 1900 0.5 32 4:1 r/m-EB(4-Ph-2-Ind)2ZrCl2 4.0 5000 0 60 1.8 5 — 3000 9.9 33 ″ 0.5 40000 2.7 60 15.1 330 — 1300 0.2 34 7:3 r/m-EB(4-Ph-1-Me-2- 4.0 5000 0 30 246 1350 — 15500 0.4 Ind)2ZrCl2 35 7:3 r/m-EB(4-Ph-1-Me-2- 0.5 40000 2.7 60 49 1070 — 1000 0.1 Ind)2ZrCl2 36 m-EB(4-Ph-1-Me-2-Ind)2ZrCl2 4.0 5000 0 60 101 280 — 15100 <0.1 37 ″ 0.5 40000 2.7 60 41 900 — 1000 0.2 38 r-EB(1-Et-2-Ind)2ZrCl2 4.0 5000 0 60 2.5 7 — — — 39 ″ 0.5 40000 2.4-3.6 60 60.2 1320 — 1000 0.5 40 m-EB(1-Et-2-Ind)2ZrCl2 4 5000 0 60 4 11 — 3700 0.9 41 ″ 0.5 40000 2-2.5 60 231 5080 — 1800 0.3 -
TABLE 5 Ethylene/propylene copolymerization Metallocene Al/Zr C2H4 H2 Time Yield Activity I.V.* C3 Ex. Type μmol mol/mol (mol %) (mol %) (min) (g) (Kg/gZr · h) (dl/g) (mol %) 42 EB(2-Ind)2ZrCl2 4.0 1000 5.6 0 40 225 920 0.46 19.0 43 ″ 2.0 40000 5.6 0 45 44.5 1300 0.47 13.8 44 r-EB(1-Me-2-Ind)2ZrCl2 0.47 42900 5.5 0 47 290 8660 0.69 23.4 45 ″ 0.94 21500 5.5 0 17 260 10660 0.71 17.9 46 m-EB(1-Me-2-Ind)2ZrCl2 1.0 20400 5.5 0 33 250 4992 0.53 24.1 47 r-EB(1-Et-2-Ind)2ZrCl2 0.5 40200 6.2 0 65 181 6400 0.93 26.9 48 m-EB(1-Et-2-Ind)2ZrCl2 0.5 40200 6.2 0 60 570 12500 0.63 23.3
Claims (28)
1. A bridged zirconocene compound of formula (I):
wherein R1, R2, R3 and R4, the same or different from each other, are selected from the group consisting of hydrogen, linear or branched, saturated or unsaturated, C1-C20 alkyl, C3-C20 cycloalkyl, C6-C20 aryl, C7-C20 alkylaryl and C7-C20 arylalkyl radicals, optionally containing one or more Si or Ge atoms, or wherein two substituents of R1, R2, R3 and R4 form a ring having from 4 to 8 carbon atoms;
R5 and R6, the same or different from each other, are selected from the group consisting of linear or branched, saturated or unsaturated C1-C20 balky, C3-C20 cycloalkyl, C6-C20 aryl, C7-C20 alkylaryl and C7-C20 arylalkyl radicals, optionally containing one or more Si or Ge atoms, or wherein two vicinal R6 substituents on the same indenyl group form a ring having from 4 to 8 carbon atoms;
m is an integer ranging from 0 to 2; n is an integer ranging from 0 to 4;
the groups X, the same or different from each other, are hydrogen, halogen, —R, —OR, —SR, —NR2 or —PR2, wherein R is selected from the group consisting of linear or branched, saturated or unsaturated, C1-C20 alkyl, C3-C20 cycloalkyl, C6-C20 aryl, C7-C20 alkylaryl and C7-C20 arylalkyl radicals, optionally containing one or more Si or Ge atoms.
2. The bridged zirconocene compound according to claim 1 , characterized in that R1, R2, R3 and R4 are selected from the group consisting of hydrogen, methyl, ethyl, propyl, phenyl and benzyl.
3. The bridged zirconocene compound according to claim 2 , characterized in that R1, R2, R3 and R4 are hydrogen.
4. The bridged zirconocene compound according to claim 1 , characterized in that R5 and R6 are selected from the group consisting of methyl, ethyl, propyl, phenyl and benzyl.
5. The bridged zirconocene compound according to claim 1 , characterized in that X is selected from the group consisting of Cl, Br and methyl.
6. The bridged zirconocene compound according to claim 1 , characterized in being selected from the group consisting of 1,2-ethylene-bis(2-indenyl)zirconium dichloride and dimethyl,
1,2-ethylene-bis(1,3-dimethyl-2-indenyl)zirconium dichloride and dimethyl, rac- and meso-1,2-ethylene-bis(1-methyl-2-indenyl)zirconium dichloride and dimethyl, rac- and meso-1,2-ethylene-bis(1-ethyl-2-indenyl)zirconium dichloride and dimethyl, rac- and meso-1,2-ethylene-bis(4-phenyl-2-indenyl)zirconium dichloride and dimethyl, rac- and meso-1,2-ethylene-bis(1-methyl4-phenyl-2-indenyl)zirconium dichloride and dimethyl, rac- and meso-1,2-ethylene-bis(1-isopropyl-4-phenyl-2-indenyl)zirconium dichloride and dimethyl.
7. A catalyst for the polymerization of olefins comprising the product obtainable by contacting:
(A) one or more bridged zirconocene compounds of formula (I), as described in any of claims 1 to 6 , and
(B) a suitable activating cocatalyst.
8. The catalyst according to claim 7 , characterized in that said activating cocatalyst is a linear, branched or cyclic alumoxane, containing at least one group of the type:
wherein the substituents R8, the same or different from each other, are linear or branched, saturated or unsaturated C1-C20 alkyl, C3-C20 cycloalkyl, C6-C20 aryl, C7-C20 alkylaryl, C7-C20 arylalkyl radicals, or groups —O—Al(R8)2.
9. The catalyst according to claim 8 , characterized in that said alumoxane is selected from the group consisting of methylalumoxane, tetra-isobutyl-alumoxane, tetra-2,4,4-trimethylpentylalumoxane, tetra-2-methyl-pentylalumoxane and mixtures thereof.
10. The catalyst according to claim 7 , characterized in that said activating cocatalyst is the product of the reaction between water and an organometallic aluminum compound of formula AlR8 3 or Al2R8 6, wherein the groups R8, the same or different from each other, are a linear or branched, saturated or unsaturated C1-C20 alkyl, C3-C20 cycloalkyl, C6-C20 aryl, C7-C20 alkylaryl or C7-C20 arylalkyl groups.
11. The catalyst according to claim 7 , characterized in that said activating cocatalyst is a compound capable of forming an alkyl zirconocene cation, having formula Y+Z−, wherein Y+ is a Bronsted acid and Z− is a compatible non coordinating anion.
12. A process for the polymerization of olefins comprising the reaction of polymerization of one or more olefinic monomers in the presence of a catalyst as described in any of claims 7 to 11 .
13. The process according to claim 12 , characterized by being used in ethylene homopolymerization or in the copolymerization of ethylene with propylene, 1-butene, 1-hexene, 4-methyl-1-pentene or 1-octene.
14. The process according to claim 12 , characterized by being used in propylene homopolymerization, in the presence of hydrogen, in amounts ranging from 1 to 30 mol % with respect to the total quantity of hydrogen and propylene, at 50° C.
15. A ligand of formula (II):
wherein R1, R2, R3, R4, R5 and R6, m and n have the meanings reported in any of claims 1 to 4 , with the provisos that:
when R1, R2, R3 and R4 are hydrogen and n is 0, then m is different from 0; and
when R1, R2, R3 and R4 are hydrogen, n is 0 and m is 1, then R5 is different from —CH3, —CH2Ph and —Si(CH3)3.
16. A process for the preparation of a ligand of formula (II), as described in claim 15 , comprising the following steps:
(1) reacting an adipic ester of formula (III):
wherein R1, R2, R3 and R4 have the meaning reported in claim 1 and R7 is selected from the group consisting of linear or branched, saturated or unsaturated C1-C20 alkyl, C3-C20 cycloalkyl, C6-C20 aryl, C7-C20 alkylaryl and C7-C20 arylalkyl radicals; with at least 2 equivalents of a benzyl compound of formula (IV):
wherein R6 and n have the meaning reported in claim 1 and Y is a leaving group; and with at least 2 equivalents of an alkali metal or alkaline earth metal base, in the presence of an organic solvent, to obtain an intermediate compound of formula (V):
wherein R1, R2, R3, R4, R6, R7 and n have the meaning reported above;
(2) converting the compound of formula (V), obtained from step (1), to a compound of formula (VI):
wherein R1, R2, R3, R4, R6 and n have the meaning reported above and Y′ is a leaving group, and cycling said compound of formula (VI) to obtain a compound of formula (VII):
wherein R1, R2, R3, R4, R6 and n have the meaning reported above;
(3) reducing, the ketonic functions on the indanyl moieties of the compound of formula (VII), obtained from step (2), to obtain a diol (VIII):
wherein R1, R2, R3, R4, R6 and n have the meaning reported above, and finally dehydrating the hydroxy functions on the indanyl moieties of said diol (VIII) to give said ligand (II).
17. The process according to claim 16 , characterized in that, when m ≠ 0 in formula (II), R5 is introduced on the cyclopentadienyl ring by reacting said compound of formula (VII) or said ligand of formula (II) with at least 2 equivalents of an alkylating agent R5MgBr, R5MgCl or R5 jB, wherein B is an alkaline or alkaline-earth metal and j is 1 or 2, at a temperature ranging from −78° C. to 20° C., for a time of 1-3 hours, in the presence of an organic solvent.
18. The process according to claim 16 , characterized in that, in step (1), said adipic ester of formula (III) is reacted with 2-4 equivalents of said compound of formula (IV) and 2-4 equivalents of said alkali metal or alkaline earth metal base, by sequential addition of said base and of the benzyl compound of formula (IV), in the presence of an organic solvent, at a temperature ranging from 20 to 80° C.
19. The process according to claim 18 , characterized in that said base of an alkali metal or alkaline earth metal is selected from the group consisting of NaOEt, KOEt, NaOH, KOH, NaH, KH and mixtures thereof, and said organic solvent is THF, glyme and/or toluene.
20. The process according to claim 16 , characterized in that step (2) comprises first de-esterifying the functions —COOR7 of the compound of formula (V) to the corresponding —COOH groups, by adding at least 2 equivalents of a base in a mixture of aqueous and organic solvents, at a temperature ranging from 20 to 150° C., for a time of 1-5 hours; then derivatizing said —COOH groups with a suitable leaving group Y′ and finally cycling the compound of formula (VI) to the compound of formula (VII).
21. The process according to claim 20 , characterized in that said base is KOH and/or NaOH, said mixture of solvents is a mixture of water and MeOH, and the deesterification is carried out at a temperature ranging from 70 to 100° C., for a time of 2-3 hours.
22. The process according to claim 20 , characterized in that said group Y′ is Cl or Br.
23. The process according to claim 22 , characterized in that Y′ is Cl and the compound of formula (VI) is obtained by reacting said —COOH groups with SOCl2 in amounts ranging from 6 to 10 equivalents per Y′ group, at a temperature ranging from 20 to 80° C., for a period of 4-12 hours.
24. The process according to claim 20 , characterized in that said compound of formula (VI) is cycled to the compound (VII) with 1.1-1.3 equivalents of AlCl3, at a temperature of 0-40° C., in the presence of an organic solvent.
25. The process according to claim 16 , characterized in that, in step (3), said compound (VII) is reduced to the diol (VIII) by reaction with 1.0-1.2 equivalents of a reducing agent selected from the group consisting of NaBH4, LiAlH4, NaH and KH, in MeOH, at a temperature ranging from −20° C. to 20° C.
26. The process according to claim 16 , characterized in that, in step (3), said diol (VIII) is dehydrated to the ligand (II) by treatment with catalytic amounts of p-toluensulfonic acid or HCl, in an organic solvent, at a temperature ranging from 20 to 100° C.
27. The process according to claim 16 , characterized in that, in step (3), said diol (VIII) is dehydrated to the ligand (II) by thermolysis, at a temperature ranging from 200 to 300° C., for a period of 1-2 hours.
28. A compound of formula (V):
wherein R1, R2, R3, R4, R5, R6 and n have the meaning reported in any of claims 1 to 4 , and R7 is selected from the group consisting of linear or branched, saturated or unsaturated C1-C20 alkyl, C3-C20 cycloalkyl, C6-C20 aryl, C7-C20 alkylaryl and C7-C20 arylalkyl radicals.
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Application Number | Title | Priority Date | Filing Date |
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US09/265,046 Expired - Fee Related US6232484B1 (en) | 1998-03-09 | 1999-03-09 | Bridged zirconocene compounds, process for their preparation and their use as catalyst components in the polymerization of olefins |
US09/795,894 Expired - Fee Related US6306791B2 (en) | 1998-03-09 | 2001-02-28 | Bridged zirconocene compounds, process for their preparation and their use as catalyst components in the polymerization of olefins |
US09/972,336 Expired - Fee Related US6673880B2 (en) | 1998-03-09 | 2001-10-05 | Bridged zirconocene compounds, process for their preparation and their use as catalyst components in the polymerization of olefins |
Family Applications Before (2)
Application Number | Title | Priority Date | Filing Date |
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US09/265,046 Expired - Fee Related US6232484B1 (en) | 1998-03-09 | 1999-03-09 | Bridged zirconocene compounds, process for their preparation and their use as catalyst components in the polymerization of olefins |
US09/795,894 Expired - Fee Related US6306791B2 (en) | 1998-03-09 | 2001-02-28 | Bridged zirconocene compounds, process for their preparation and their use as catalyst components in the polymerization of olefins |
Country Status (4)
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US (3) | US6232484B1 (en) |
JP (1) | JP2000053691A (en) |
DE (1) | DE69904521T2 (en) |
ES (1) | ES2188047T3 (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US9884925B2 (en) | 2014-04-17 | 2018-02-06 | Oxford University Innovation Limited | Silyl bis(hexamethylindenyl) complexes of group IVA metals as polymerization catalysts |
US10221259B2 (en) | 2015-01-06 | 2019-03-05 | Scg Chemicals Co., Ltd. | SiO2-layered double hydroxide microspheres and their use as catalyst supports in ethylene polymerisation |
US10773246B2 (en) | 2015-01-06 | 2020-09-15 | Scg Chemicals Co., Ltd. | SiO2-layered double hydroxide microspheres and methods of making them |
US11053269B2 (en) | 2016-05-12 | 2021-07-06 | Scg Chemicals Co., Ltd. | Unsymmetrical metallocene catalysts and uses thereof |
Families Citing this family (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6342622B1 (en) * | 1999-06-11 | 2002-01-29 | Dsm B.V. | Indenyl compounds for the polymerization of olefins |
CN1374973A (en) * | 1999-09-22 | 2002-10-16 | 巴塞尔技术有限公司 | Catalyst system and process for polymerization of olefin(s) |
WO2003008465A2 (en) * | 2001-07-19 | 2003-01-30 | Univation Technologies, Llc | Low comonomer incorporating metallocene catalyst compounds |
US6559251B1 (en) * | 2002-08-02 | 2003-05-06 | Equistar Chemicals, Lp | Process for making low-density polyolefins |
US7176158B2 (en) * | 2002-10-25 | 2007-02-13 | Exxonmobil Chemical Patents Inc. | Polymerization catalyst composition |
CN100457789C (en) * | 2004-10-27 | 2009-02-04 | 中国石油化工股份有限公司 | Catalyst components for olefinic polyreaction and catalyst thereof |
ES2322275T3 (en) * | 2005-08-17 | 2009-06-18 | Saudi Basic Industries Corporation | COMPOSITION OF CATALYST FOR RESIN POLYMERIZATION, POLYMERIZATION PROCESS USING THE SAME, AND METHOD FOR PREPARATION. |
IN2014DN04977A (en) * | 2011-12-19 | 2015-05-15 | Saudi Basic Ind Corp Sabic | |
JP6454548B2 (en) * | 2011-12-19 | 2019-01-16 | サウディ ベーシック インダストリーズ コーポレイション | Process for preparing metallocene complexes |
JP6326202B2 (en) * | 2013-05-16 | 2018-05-16 | 三井化学株式会社 | Solid catalyst component for olefin polymerization and process for producing olefin polymer using the same |
CN104370681A (en) * | 2014-09-29 | 2015-02-25 | 中国科学院上海高等研究院 | Synthesis method of vinyl-bridged dialkylindene compound |
US10889662B2 (en) | 2014-12-12 | 2021-01-12 | Lg Chem, Ltd. | Metallocene-supported catalyst and method of preparing polyolefin using the same |
US11155659B2 (en) * | 2017-04-04 | 2021-10-26 | Sabic Global Technologies B.V. | Dimethyl-silyl-bridged-1-substituted-2-indenyl metallocene complexes for olefin polymerization |
CN110650965B (en) | 2017-04-04 | 2022-10-04 | Sabic环球技术有限责任公司 | Dihydrocarbyl-silyl-bridged-1,3-disubstituted-2-indenyl metallocene complexes for olefin polymerization |
EP4110834B1 (en) | 2020-02-24 | 2024-04-03 | ExxonMobil Chemical Patents Inc. | Ansa-bis(inden-2-yl) catalysts for producing vinylidene-terminated polyalphaolefins |
Family Cites Families (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE3840772A1 (en) | 1988-12-03 | 1990-06-07 | Hoechst Ag | METHOD FOR PRODUCING A HETEROGENIC METALLOCENE CATALYST COMPONENT |
DE59104869D1 (en) | 1990-11-12 | 1995-04-13 | Hoechst Ag | 2-Substituted bisindenyl metallocenes, process for their preparation and their use as catalysts in olefin polymerization. |
NL9201970A (en) * | 1992-11-11 | 1994-06-01 | Dsm Nv | Indenyl compounds and catalyst components for the polymerization of olefins. |
IT1290856B1 (en) * | 1996-12-19 | 1998-12-14 | Enichem Spa | METALLOCENES, THEIR PREPARATION AND USE IN THE POLYMERIZATION OF ALPHA-OLEFINS |
DE69907785T2 (en) * | 1998-03-09 | 2004-02-12 | Basell Poliolefine Italia S.P.A. | Multi-stage process for olefin polymerization |
-
1999
- 1999-03-03 ES ES99104222T patent/ES2188047T3/en not_active Expired - Lifetime
- 1999-03-03 DE DE69904521T patent/DE69904521T2/en not_active Expired - Fee Related
- 1999-03-09 US US09/265,046 patent/US6232484B1/en not_active Expired - Fee Related
- 1999-03-09 JP JP11062448A patent/JP2000053691A/en not_active Withdrawn
-
2001
- 2001-02-28 US US09/795,894 patent/US6306791B2/en not_active Expired - Fee Related
- 2001-10-05 US US09/972,336 patent/US6673880B2/en not_active Expired - Fee Related
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US9884925B2 (en) | 2014-04-17 | 2018-02-06 | Oxford University Innovation Limited | Silyl bis(hexamethylindenyl) complexes of group IVA metals as polymerization catalysts |
US10221259B2 (en) | 2015-01-06 | 2019-03-05 | Scg Chemicals Co., Ltd. | SiO2-layered double hydroxide microspheres and their use as catalyst supports in ethylene polymerisation |
US10773246B2 (en) | 2015-01-06 | 2020-09-15 | Scg Chemicals Co., Ltd. | SiO2-layered double hydroxide microspheres and methods of making them |
US11643331B2 (en) | 2015-01-06 | 2023-05-09 | Scg Chemicals Co., Ltd. | SiO2-layered double hydroxide microspheres and methods of making them |
US11053269B2 (en) | 2016-05-12 | 2021-07-06 | Scg Chemicals Co., Ltd. | Unsymmetrical metallocene catalysts and uses thereof |
Also Published As
Publication number | Publication date |
---|---|
US6673880B2 (en) | 2004-01-06 |
US20010014751A1 (en) | 2001-08-16 |
US6306791B2 (en) | 2001-10-23 |
DE69904521D1 (en) | 2003-01-30 |
US6232484B1 (en) | 2001-05-15 |
ES2188047T3 (en) | 2003-06-16 |
JP2000053691A (en) | 2000-02-22 |
DE69904521T2 (en) | 2003-10-02 |
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